HomeMy WebLinkAboutAPA3015PLACER MINING W ASTEW )~ TER
SETTLING POND
DEMONSTRATION PROJE ~CT
REPORT
Prepared For:
State of Alaska
Department of Environmental Conservation
Pouch 0
Juneau, AK. 99811
June, 1982
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Susitna Joint Venture
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DOCUMENT CONTROL
PLACER MINING WASTEWATER
SETTLING POND
DEMONSTRATION PROJECT
REPORT
Prepared For:
State of Alaska
Department of Environmental Conservation
'Pouch 0
Juneau, AK. 99811
June, 1982
PLACER MINING WASTEWATER
SETTLING POND
DEMONSTRATION PROJECT
Prepared Fo~:
State of Alaska
Department of Environmental Conservation
June, 1982
Prepared By:
R & M Consultants, Inc.
711 Gaffney
Fairbanks, Alaska 99701
Although this investigation described herein has been partially funded by the
U. s. Environmental Protection Agency through Grant No P-000179-01-0 to the
Alaska Department of Environmental Conservation, it has not been subjected to
the Agencyrs peer and administrative review and therefore does not necessarily
reflect the views of the Agency, and no official endorsement should be inferred.
TABLE OF <XNIENTS
Page No.
SEcriON ONE -INI'R:IXJC!'IC!l
1.1
1.2
1.3
1.4
1.5
1.6
2.3
2.4
2 .• 5
.... 1 _,., 4
3.2
3.3
3.4
3.5
3.6
3.7
3.8
3.9
Progrant Objectives and Goals ••••••••••••••••••••••••••••••••••••• !
Scope of Study ••••••••••••••••••••• ~······•••••••••••Q•••••••••••2
Background and Histo~··•••••••••••••••••••••••••••••••••••••••••4
Characteristics of Placer Mines ••••••••••••.• 0 e ••••• iii •••••• II •••••• 6
Previous Studies •••••• $ •••••••••••••••••••••••••••••••••••••••••• 7
State cu"'ld Federal Watf!r Quality Standards and Effluent
Guide1ines ••• Q•••••••••••••••••••••••••••••••••••••••••••••••••••9
Settling Column Test Procedures and Objectives •••••• ~···········l2
Porc~ine Creek Settling Column Test ••••••••••••••• Q •••••••••••• l3
Settling CoJ.umn Tests for Individual Mine Sites ••••••••••••••••• 13
Results ••••••••••••••••••••••••••••••••••••••••••••••••••••••••• l4
Conclusions ••••••••••••.• G ••••• " ••••••••• "' •••••••••••••••••••••• !17
General Objectives •••••••••••••••••••••••••• Q ••••••••••••••••••• l9
Field Investigation~··••e••••o••••••••••••••••••••••••••••••••••l9
Pol1c1 Ilesign ....................................... 1J •••••••••••••• 21
PQ~ Construction And Maintenance~·········~····················23
Mine Operations •••• ~············································24
Pond Modification ••••••••••••••••••••••••••••••••••••••••••••••• 26
Data Coll~-tion ••••••••••••••••••••••••••••••••••••••••••••••••• 27
Results ••••••• ., ••••••••••••••••••••••••••••••••••••••••••••••••• 28
s~ of Data ••••••••••••••••• ~ ••••••••••••••••••••••••••••••• 28
Natural Water Quality •••••••••••••••••••• Q •••••••••••••••••••••• 29
Pond Flow Measurements ........................................ r •• 30
Effect of Mine Operatians~··••••••••••••••••••••••s•••••••••••••30
Effectiveness of Tailrace and Pond •••••••••••••••••••••••••••••• 31
Pond Modifications •••••••••••••••••••••••••••••••••••••••••••••• 33
Corlclusioos .................................................. e ••• 34
SECI'IOO FOOR-INDIVIIXTAL MINE SURVEY
4.1
4.2
4.3
4.4
4.5
General•s••••••••••••••••••••••••••••••••••o•••••••••••••••••••••37
(JI:)jectives ••••••••••••••••••••••••••••••••••••••••••••••••••••••• 37
Mirle O};'erations ••••••••••••••• !t •••••••••••••• c-•••••••••••••••e•••38
sampling and Testing ••••••••••••••••••••••••••••••••••• ~·········40
Resu1ts ••••••••••••••••••• ~••••••••••••••••••o•••••••••••••••••••42
Natural Water Quali~···•••••••••••••••••••••••••••••••••••••••••42
Effects of Placer Mining on Natural Water Quality ••••••••••••• ~ •• 43
Effects of SUrface I:Alacilg of Settling Ponds on Sedimentation ••••• 46
Effects of Particle Sizes on Sedimentation ••••••••••••••••••••••• 47
i
t
f
Hater Use •••• ~··••••••••••••••••••••••••a•••··~~·-··~··••••••••••52
4.6 Ca'lcl.usi()l'18 ....................................................... 54
SECri<E FIVE -SU!ti4ARY
5.1
5.2
Catpliance Wi tll St:anc!ards .......................................... 57
Sedilnentation Efficiency ••• " ••••••••••••••••••••••••••••••••••••• sa
ii
Table 1
Table 2
Table 3
Table 4
Table 5
Table 6
Table 7
Table 8
Table 9
Table 10
Table 11
Table 12
Table 13
Table 14
Table 15
Table 16
Table 17
Drawing 1
Drawing 2
Drawing 3
Drawing 4
Drawing 5
Drawing 6
Drawing 7
Drawing 8
Drawing 9
Drawing 10
Drawing 11
Drawing 12
Drawing 13
Drawing 14
Drawing 15
Drawing 16
Drawing 17
Drawing 18
Drawing 19
LIS!' OF TABLES
Average Total Suspended Solids and Turbidity Values Settling Colunn Tests
Water Quality Data Collected August 14, 1980
Water Quality Data From Sampling Sites Located Upstream of Mine 16
Water Quality Data Fran Mine 16 Sampling Sites
Mine Site Locations
Equipnent at Selected Placer ~line Sites
SUmmary of Mine Operations
Water Use and Settling Pond Characteristics
Ranges and Means of Measured Parameters Above, Wit~n and Below
Placer Mines
Arsenic Concentrations at 15 Mine Sites
Arsenic Conditions for Various Conditions at Placer Mine Sites
Dissolved and Suspended Arsenic Mean Coocentrations and Standard
Deviation For Various Conditions at Placer Mines
Sedimentation Effectivness at Surveyed Placer Mines
Particle Size Analysis of Material From Paydirt
Distribution of Particle Sizes of Fraction Passing No. 50 Sieve
.Sedfmentation Characteristics of Settling Ponds at surveyed Placer Mines
Manning's 11 n fj( Value For Selected Sluice Box
Lisr OF DFAW:Q~;S
Location of Project Areas
Location of Placer Mines Sampled
Settling CollJlU'l Data
Percent Ranoval of Suspended Solids
Relationship Between ntrbidity and Total Suspended Solids
Demonstration Sett!ling Pond and Benn
Sampling Sites, Denonstration Settling Pond
Effect of Benn Placenent on Settleable Solids
Grain Size CUrves, Porcupine Creek Site
Grain Size CUtves, z.t..ine Sites 1-5
Grain Size curves, Mine Sites 6-10
Grain Size CUrves, Mine Sites 11-14
Effect of Particle Size on Settling Pond Efficienqy
Particle Settling Velocites
Relationshi~ Between Settling Velocity and Renoval of Total Suspended
Solids Mines 1 and 2
RelationshiiE Between Settling Velocity and Refnoval of Total Suspended
Solids Mines 3 and 4
Relationships Between Settling Velocity and Ranoval of Total Suspended
Solids Mines 5 and 6
Relationshii=S Between Settling Velocity and Removal of Total Suspended
Solids, Mines 7 and 8
Relationshi};S Between Settling Velocity and Ranoval of Total Suspended
Solids, Mine 9 and 10 -
iii
Drawing 20
Drawing 2l
Drawin.g 22
Drawing 23
Drawing 24
Drawinq 2!5
Drawing 2(:;
Drawing ZJ'
Appendi.x I
~dix II
Appendix III
~dix rv
Relationshipa Setween Settling Velocity and Ranoval. of Total suspended
Solids, Mine 11 and 12
Relatioo~!l=t Between Settling Velocity and Renoval of TOtal suspended
Solids, r-tine 13 and 14·
Relationshite Between settling . -.elocity and Removal of Total Suspended
Solids, Mine 15 and 16
Placer Mine Water Usage, Mines 1 through 4
Placer Mine Water Usage, Mines 5 and 6
Placer Mine Water Usage, Mines 7 through lOA
Placer Mine Water Usage, Mines lOB through 12
Placer Mine Water Usage, Mines 13 and l4
Settling CollJIU'l Data, Individual Mine Sites
Sample Site Descriptions and Methods of Data Collection
Porcupine Creek 50 Day Sampling Data
Individual Mine Site Data
iv
SEcriON ONE
IN'J.R)D{Jcr'ION
1.1 .FJ.INRAM QPJECriVES AW ro&8
This report presents the results of a study conducted by R & M Consultants,
me. on the effectiveness of settling ponds for treatment of effluent water
from AJ.aska placer gold mines.. As part of this study, a demonstration
settling pond was designed, constructed at an operating mine on Porcupine
creek (near Central, Alaska), and monitored for SO days during the 1981
mining season. In addition, the water quality at fifteen other mine sites,
including a mine above the demonstration site, was periodically sampled
during the 1981 mining season. The data collected in these efforts are
presented in thi~ report, together with the evaluation and conclusions that
have been derived from these data.
This study had as its objectives::
1. Design and construction of a demonstration settling pond that could
provide a high level of treatment of placer mining discharges.
2. Evaluation of the effectiveness of the demonstration settling pond
in improving the quality of placer mining discharges, including
comparison of actual water quality to EPA effluent guidelines and
state water quality standards for turbidity, suspended solids and
settleable solids, I;ii, temperature, dissolved oxygen, and chemical
o.xygen demand.
3. Evaluation of the economics of construction, operation,
l
maintenance, and closeout of the demonstration settling p:>oo.
4. Collection of information to compare settling pond performance at a
number of different placer mines having differing methods of mining
operations and differing characteristics of the material being
mined, relative to the demonstration :pond.
5. Definition of the water quality of the discharge of placer mines
that do not use settling pooos for ranoval of suspended materials.
t5. Measurement of water used by placer mining operations to provide
infon~ation for defining water u$age and for evaluating water use
permit cq;:plications.
7. Preparation a sediment control handbook from the information
gathered by this study for use by to the mining iooustry.
1.2 .~'IDPE QE gmpx
The iuitial scope of this study, as defined by the Alaska Department of
Environmental Conservation, ("ADEC") included the design, construction,
monit:oring and evaluation of effectiveness of a settling pond that would
theor4!tically provide the best achievable sediment control treatment possible
using a conventional settling pond. The settling pond effluent was to be
monit:ored for dissolved oxygen, water temperature, pH, settleable solids,
total suspended solids, turbidity and chemicc.l oxygen demand at selected
flows ..
The s:cope of this study specifically did not include the evaluation of
2
partial recyclin~hemical flocculants or mechanical methods in treating
placer min i.ng effluents •
.Becac e few mines in the Circle Mining District used settling ponds, the
Distri' 't was chosen for the demonstration project. After solicitation, only
two mir.~. "'rs volunteered their operations, and the Porcupine Creek site was
therefore selectea by the D.E.C.
The scope of the study was amended after a public meeting with interested
parties. The general consensus was that studying one site would define
conditions at only one mine in a highly variable industry and that the
effectiveness of sediment control at a number of mi~e sites should be
,evaluated. To meet these concerns, the study was amended to reduce sampling
at the Porcupine Creek site from 100 days,· as initially planned, to 50 days
and to .include fifteen additional mine sites to be sampled on three separate
occasions. The revised scope included:
1 e Rep:>rting the following for each mine site: type of equipment used,
volume of material moved, the size and distribution of soil
:r;articles in the p:tydirt, the method used to process paydirt, and
the quanti~ of water used to process a given volume of materialo
2. Reporting the type of wastewater treatment used by each miner,
including size of settling pond, if any, and extent of water reuse.
3. Monitoring water quality during each visit, including measurement
o:f: -t:lissol ved oxygen, water temperature, pH, settleable solids,
total suspended solids and turbidity. Tbtal and dissolved arsenic
was to be sampled during one visit at each mine.
3
4. Performing settling column tests on materia.! collected from the
sluice b.")x discharge at each mine site.
The scope was further enlarged to obtain data requested by the Alaska Depart-
mEa"'lt of Natural Resources to use in evaluation of water permit applications
submitted by minerso This included collection of data for computation of
Manning's roughness coefficient "n 11 for the sluice boxes of each miner.
Also, flow measurements of the stream and mine operation were to be made to
permit the computation of the water bR!ance of each mine site to determine
consumptive use, if any.
The sixteen mine sites, including the demonstration settling pond site, were
ctosen by the ADEC based on their location, type of operation and willingness
to participate in the study. Although seventeen mines were initially
sampled, only sixteen sites were sampled throughout the 1981 mining seas~
Dr.awings 1 and 2 show the locations of the mine sites studied.
1.3 BACXC;BXJNP Mil HISJDRY
Gold m.ining was the cornerstone of the economy in Interior Alaska, beginning
in the latter part of the nineteenth century through the 1930"s. Gold mining
decreased after ~Jorld War II until, by the early 1970's, there were fewer
than 200 active placer mines in the State.. The subsequent increase in the
price of gold caused a significant resurga1ce in the n~~ber of active placer
operations in Alaska in the past few years. This increase in activity has
4
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lileru, • ., I
E A
OftAWtN~ I
LOCATION ~ ,.,_,ECT AIEAS
( PlltOM U S6S AI..AIKA ... C )
...... •
DRAWI~G 2
POND DEMONSTRATION PROJECT
N
NOTE:
LOCATION OF PLACER MINES SAMPLED
~ ----"'·---~· ·--------.
been paralleled by a gr01wing concern about the effects of placer mining on
water quality and the corresponding effects on fish and other aquatic life
and on commercial and ptiJlic uses of surface waters.
Gold is typically located in relatively thin layers of gravel covered by a
few feet to many tens of feet of overburden, depending on the area. OVer-
burderi is removed and the g1~ld-bearing strata is washed through a sluice box
to separate the gold. The major cause of water quality degradation by placer
gold mining is the discharge of sediment-laden water from mining operations
into a stream. Seconda~ causes of water quality degradation include strip-
ping operations for removing overburden, erosion of tail.inqs, and, in some
areas, leaching from the tailings pile~
Stream sedimentation and the associated turbidity caused by placer mining is
the most visible concern related to water quality. Sedimentation and
turbidity are usually not confined to the immediate area or reach of the
stream where mining occurs, but can persist for some distance downstream.
Sedimentation and turbidity can affect fish and other aquatic biota by
smothering aquatic life such as fish eggs and the benthic organisms on which
fish fee(L Cordone and Kelley (1960) reviewed a fairly voluminous amount of
literature showir~ that seCimentation and turbidity can not only affect fish
and other aqua·tic biota by smothering of fish eggs and the benthic organisms
on which fish feed, but also can affect growth rates and feeding habits of
fish. &1en if turbidity levels are not so high as to clog the gills of fish,
evidence exists that silt-sized particles of hardness greater than one can
cause gill damage through abrasive or matting actioo.
5
The same authors endorse the statement that N_ adequate data are not
available on the amounts of inorganic materials which can be added to a
stream without significant harm to its productive capacity," and conclude
that while ftsediment problems---related to gravel and mining operations are
often spectacular, they are probably less important than gradual deposition
due to erosioo" o Turbidity can also affect the recreation use of stream and
river waters.
1.4 QiAPACl'ERISTICS Of PLN:fiR MINES
Placer mining operations are so variable that one could state that the only
constant among operations is that each mine site has site specific
coooitions. The variability results from a number of factors, including, but
not necessarily limited to:
physical location,
size of operatioo,
amotmt and type of overoorden,
width of gold-bearing strata,
-equipoent and type of material processing,
water availability and use,
degree of water reuse or recycling,
degree of wastewater treatment, and
condition (clear vs. glacial) and size of source water and
receiving stream.
All of the above factors may in some way be related to the potential for
water quality degradation below the mine site. M~ny of these factors are
6
The same authors endorse the statement that "-adequate data are not
available on the amounts of inorganic materials which can be added to a
stream without significant harm to its productive capacity," and conclude
that while "sediment problems---related to gravel and mining operations are
often spectacular~ they are probably less important than gradual deposition
due to erosioo". Turbidity can also affect the recreation use of stream and
river waters~~
Placer mi.."ling operations are so variable tha't one coUld state that the only
constant among operations is that each mine site has site speciflc
conditions. The variability results from a number of factors, including, but .
not necessarily limited to:
-
·-
physical location,
size of operaticn,
amount and t~ of overoorde.n,
width of gol~ring strata,
equipnent and type of material processing,
water availability and use,
degree of water reuse or recycling,
degree of wastewatex; treatment, and
condition (clear vs. glacial) and size of source water and
receiving stream.
All of the above factors may in some way be related to the {X>tential for
water quality degradation below the mine site. MS!nY of these factors. are·
6
interrelated and some may dictate the type of mining operation. For example,
size of operation may be a function of the availability of water anq/or the
type of equipment used by the miner. Wate.c availability may also influence
the method of overburden removal, i.e., hydraulic or mechanical, an~ the
specific operating mode of the mine. For example, the removal of ov~~size
material prior to sluicing results in less water being required to move the
gold-bearing material through the sluice box. Full or partial reuse of
sluice water is another common method of reducing water use.
Primary equipmE.'nt for moving material may consist of one type, or a combina-
tion of many types, such as hydraulic giants, front-end· loaders, backhoes,
dozers, scrapers, draglinea, or dredges. Consequently, it "!ould be difficult
to find two identical placer gold mining operations in Alaska.
The effects of placer mining on water quality has been a topic of few in-
depth studies. Generally these studies are classified into two groups: short
term (one mining season) studies of a number of mine sites, or reviews of the
state of the art.
Two u.s. Environmental Protection Agency studies collected data during one
visit each to 10 and 11 mine sites, respectively. Each mine site was sampled .
at three to five locations. These studies fotmd that settling ponds do
improve water quality, but the effect of the type of mining operation anq/or
type of overburden on water quality could not be correlated. The studies
also determined that 1) estimating costs associated with mining, for
7
comparison of costs of improving water quality, is difficult at best, and 2)
a study measuring the effects of placer mining through an entire mining
season was needed (see Cal~ 1976 and 1979).
Mahc~ l l<=t ¥1 )
A Bureau of Land Managemen repor published in August, 1981 examined the
existing literature. It also proplses methodology for a short term (one to
two year) office study and a short term (one to two mining season) field
stuqy measur.ing river channel characteristics and geometry and bed-material
size and bank material size. It stresses the need for collecting data over a
full mining season rather than one visit sampling.
'!be Department of In.iian a."'ld Northern Affaire; Canada published a report in
August, 1981 on control of placer mining effluent. The conclusions of this
study are tt~t: 1) Treatment of mine effluent must be handled on a site
specific basis. 2) Although settling p::mds can I(\~Uce the concentration of
suspended solids, in most cases ponds cannot limit suspended solids
concentrations to the permitted 25-75 mg/1 rang(: \*Jithout the addition of
chemical coagulants or 3) Existing mine sites require modification of
operation prior to successful implementation of waste treatment; 4) To be
effective, site specific characteristics must be determined prior to the use
of coagulants.
In summary, previous stt.ldies oonfirm that plaa~r mining operations are highly
variable and require site specific evaluation over a full mining f)eason.
8
This section presents a discussion of State and Federal water quality stan-
dards that apply to placer mining wastewater and receiving streams bel0\\1
placer mines.
The Environmental Protection Agency has both effluent and receiving water
standards, and Alaska's water quality standards are essentially the same as
the Federal receiving water standards for most types of discharges.
Consequently, Federal permit condtt:f~ons for placer mining apply to the
effluent, whereas State standards apply to receiving water. Specific Federal
and State requirements have been presented in petmits issued to placer miners
by the u.s. &"'1vironrnental Protection .Agency in cooperation with the Alaska
Department of Environmental Conser' ation.. These specific criteria are:
Is The permittee must not cause an increase in tt.'tbidity level greater than
25 JTU (Jackson Turbidity Units) above natural turbidity in the
receiving stream at a p:>int measured 500 feet downstream of the final
dioohr,trge.
2. The petmittee must as a minimum meet one of the follow:...:~g corxlitions:
A. Pro~tide settling pond(s) which ~e design.ed to rontain the maximum
vol1.1ne of process water used during any one day's operation.
B. Provid•: treatment of process wastes such that the· ;~~::cgimum daily
concentratioh of settleable solids from the miriing of)eration shall
be 0.2 milliliter of solids per liter of effluent.
These permits also contain general provisions for effluent limitations,
9
schedule of oompliance, monitoring and reportiDJ, management requirements,
and responsibilities. These permit conditions are temporar~ pending the
outoome of an adjudicatory hearing process.
Alaska Hatet Quality Standords (ADEC 1979) must be met in addition to the
above permit requirements, and would be applied in the receiving strea.m at a
point measured 500 feet downstream of the final discharge (Brossia 1981).
'lbe following receiving water standards are presented by AD~ (1979) for the
growth and propagation of fish and other aquatic life for the parameters
measured during this study.
Dissolved r.a5. Dissolved oxygen shall be greater than 7 mg/1 in waters used
by anadromous and resident fish. For waters not used by anadromous or
resident fish, dissolved oxygen shall be greater than or equal to 5 mg/1. In
l'lO case shall dissol~ oxygen above 17 mg/1 be permitted. The concentration
of total dissolved gas shall not exceed 110 percent of saturation at ~lY
point of· saupl~ collect! at.
IlB· Shall not be less than 6.5 or greater 'than 9.0. Shall not vary more
than 0.5 :tB unit ftcm natlll'al condition. ~~
TurbiditYJ. Shall not exceed 25 NTU (Nephelometric Turbidity Units) above
natural condition level. It ~hould be noted that the permit criterion for
turbidity i~ 25 JTU. Although NTU and JTU are not directly comparable, 25
N'lU and 25 J'"ID represent roughly the same anolUlt of turbidity.
Temperature. Shall not exceed 20 °C at any time. The following maximum
10
ta'llperatures shall not be exceeded, where applicable: migration routes and
rearing areas; l5°C and spawning areas and egg fry incubation areas; l3°C.
Sediment. Tm percent accumulation of fine sediment in the range of 0.1 mm
to 4.0 nun in the gravel bed of waters utilized by· anadromous or resident fish
for spawning may not be increased more than 5% by weight over natural
conditioo (as shown from grain size accwnulation gr.aph). In no case may the
0.1 mm to 4.0 mm fine sediment range in the gravel bed of waters utilized by
anadromous or resident fish for spawning exceed a maximum of 30% by weight.
In all other surface waters no sediment loads (suspended or deposited) "'hich
can cause adverse effects on aquatic animal or plant life, their reproduction
or habitat.
.
Toxic ~ Other Deleterious Organic ~ Inorganic Substances CArsenicl&
Substances shall not individually or in combination exceed 0.01 times the
lowest measured 96 hour Lc50 for life stages of species identified by the
department as being the most sensitive, biologically important to the
location, or e~ceed criteria cited in EPA Oqality Criteria ~ Water or
AJ,a§ka Drin.Ung Water St;a@raa, whi.chever ooncentration is less. EPA (1976}
states that the drinking water standard for arsenic is 0.050 mg/1.
11
SEC!'~ 'B«>
SE'l'JLOO CDLDI'fi TmTS
One of the principal objective~ of this study was to eva1uate tbe
sedimentation rat:es of material from placer mine sluice discha.rges., This
evaluation was pe·rformed, in part, by conducting .laboratory tests usin.g
settling COl\IDllS.
The settlil'¥1 column apt:aratus consisted of 12 inch diamewr pipes ten feet in
height. sampling p>rts were located at various d~pth intervals, beginning at
a P>int one and one half feet below the top of the column. A bulk sample of
material fran the sluice box discharge was placed in the column, thoroughly
mixed, and then allowed to settle, with sample specimens taken from the
sampling ports at various time intervals over the teriod of the test. 'nlese
samples were tested :for settleable solids, suS};ellded soli,ds, and turbidity in
accordance with thte procedures specified in standar(l Metbocm La.I. .the.
Examination .Qf Water ,aDd 1{£;stewabu., 14th edition.
Settling column tests were conducted with material ootained from the sluice
box discharge at Porc~upine Cl~eek, as well as from the 14 other mines that
were surveyed in this study. The oojectives an'd prcx::edures u~ in the test
of the material from Porcupir.te Creek differed somewhat from those of the
tests of material from the other mine sites, as described below.
12
'lbe settling column test of material from Porcupine Creek was coooucted in
January and February of 1981, prior to the design of the demonstration
settling p:>m. The purpose of this test w'as to define a general relationship
between pond size and resultant levels of sediment and turbidity within the
pond effluent.
Testing was conducted at the O'lntrolled room temperature of the laboratory.
Temperature stratification was avoided by maintaining a continuous flow· of
air aroWld the column in the direction of the column axis.
Samples fran the column Tflits were d:ltained at geometrically increasing time
intervals over a 22 day test pe~iod. The total volume of material obtained
for suspended solids and turbidity testings, (five ports) caused a drop in
th~' water level in the column of about 1/4 inch (during each sampling
pedod). The total volum~ material sampled from three ports for
settleable solids tests caused the water surface to drop about two inches
each time that these samples were ct>ta.ined. Evaporation occurred at a rate
of about 1/4 inch per day. A large sample taken from the column after five
days for determination of the sizes of suspended particles caused the water
surfaa~ to drop by an additional twelve inches.
'!he objectives and methods of settling column tests that were conducted with
the material obtained from the 14 mines that were surveyed in this study
13
(other than Porcupine Creek) differed from the test of the material from
Porcupine Creek in several respects.
The objective of this testing was to determine if settling column test
results l'lOuld serve as a reliable indicator of the sedimentation rates and
turbidity reductions that could be achieved within placer mine settling
ponds. These tests, conducted during the summer of 1982, were performed in
an outdoor environment to approximate typical ambie.11t air corXiitions during
mine operations. Samples from the column parts were obtained after the
initial mixing and at 6, 12, 24, 48 and 72 t10urs after mixing. Testing was
terminated after 72 hours of sedimentation. Samples were analyzed only for
total suspended solids and turbidity.
2 .4 .BfSlLTS
Settling colwnn test results are presented in AJ;pmdix I. Turbidity values
at 1 l/2 feet am 5 l/2 feet below the initial surface of the settling colwnn
test of material from Porcupine Creek are plotted versus time in Drawing No.
3. During the first 24 lx:urs of the test the turbidity data does not show a
consistant pattern, probably because of differences in turbidity and
suspended sediment concentrations with depth at the beginning of the teste
I
After 24 hours, however, the turbidity values decrease linearly with time
when plotted on a semi logarithmic scale.
.~l( vJe~ J ......-b"l
'!be _percentage of suspended solids that was removed by sedimentation in the
settling column is shown by time am depth in Drawing No. 4.
T.he efficienqy of settling ponds at the individual mine sites was estimated
14
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•10 ..,_ to reach
2 5 flfTU SklrWard
TIM£, Hours
MGS
SETTLtNt COL DATA
PORCUPtNE CREEK
SETTLING POND DEMONSTRATION PROJECT
.,...-
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12 ______ ._ ________ ~
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T•ME, Hours
PEfltCENT REMOVAL OF SUSft£ND£D SOLIDS
SETTLtNG COLUMN DATA, PORCUPINE CREEK
SETTLING POND DEMONSTRATION PROJECT
., 2
••
950fo
[ __ 4_~_9_"':._i_·?_·. _ _...j_A_;_•_t_.~~-g·_~_N _ _.l_•_~--::_a_. _$i __ •_v_ .... r a_ ... _·•_•_j_r_w_· _._ .... ·_ '-•-~~~o.t_o_. ,_3_to'_,~._:·J ::W4~• -·)
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~----------------------------------------~------~-' --~--~----------'-----------------------------~----~----------·--------~-----------------
from the settling colmnn data by· the following procedure:
1. The fraction of p:..1rticles remaining in suspension, relative to
the average initial total suspended solids concentration in the
column, was calculated for each sample that was collected during
the tests.
2. The maximum settlin1 velocity of each sample collected during the
test was calculated by di'!Jiding the port depth below the initial
water surface in the column by the time after test startup that
each sample was oollected.
3. Ploti3 of settling velocity vs. the fraction of particles
remaining in suspension were prepared, and a least squares line in
the form P= a + b Log V was computed to fit 'the data, where P is
the percent of particles remaining in suspension, v is the settling
velocity , and a and b are regression coefficients. These plots
are included in Apperxlix I.
Data associated with settling column velocities of more than one
foot per hour were not used in computing t..he least squares equation
because of the relatively large effect on these data of initial non
uniform conditioos with depth in the column.
4. 'nle percent removal of s~nded solids can be predicted from the
I
settling column data as a function of settling veloci~ according
to the following equation:
R = 1 -~sPiN where
R = total fraction removed
V = settling velocity (corresponding to a given surface
15
overflow rate)
P = the fraction of particles remaining in suspension
By substituting the relationship between P and V described in step
(3) above, the equation becomes:
R = 1 -~ r (a + b Log V) CN
This equation was solved to predict the percentage removal of suspended
material that would occur at the individual mine sites under different
overflow rate conditions. These predictions a1:e presented in Section Four
on Drawings 15 through 22. These drawings also show the percentage removal
of susr.ended material that would be computed to occur by use of the empirical
relationship developed directly from field data, as discussed in Section
Four. The percentage removal of suspended material as predicted from the
settling column data is compared on Table 13 (See Section Four) with the
actual percentages of re:noval that were measured in the field at the settling
ponds of the individual mine sites.
Average turbidity values and total suspended solid concentrations in the
settling columns are tabulated with time for each of the surveyed mine site
in Table 1. A plot of this data in Drawing No. 5 indicates the relationship
of turbidity to the concentration of total suspended solids. The
relationship has been quantitatively defined by a least squares fit of the
data, as indicated in Drawing No. 5.
16
TABLE 1
AVERJ'.GE 'IDrAL SUSPENJED OOLIDS 1\ND 'IURBIDITY VALUES
SE'l'rLIK2 CDLUMN 'lmiS
0 BOOR 6 HOOR 12 HOUR 24 HOUR 48 HOUR 72 lkXlR
MINE TSS '1\lrb TSS '1\l.rb TSS Turb TSS Turb TSS Turb TSS Turb srm ng/1 NlU mg/1 NltJ 11Q/l NIU ~1 NID ng/1 NlU m:v'l NlU
1 6,280 3,200 2,310 2,900 2,060 2,.200 1,260 1,900 1,240 1,500 780 1,500
2 53,800 14,200 15,300 7,100 4,100 5,400 1,800 2,900 800 1,700 620 1,200
31 11,200 6,700 3,410 6,500 4,080 5,300 3,600 5,200 3,400 4,700 2v800 3,700
4 33,500 10,700 5,310 6,800 2,690 4,000 1,430 2,300 540 1,300 190 1,400
5 5,480 5,300 3,990 4,200 Zl,260 2,900 1,8'40 2,900 1,280 2,300 1,000 1,.700
6 8,100 3,100 4,250 2,300 1,850 1,600 1,410 1,300 1,130 1,100 810 1,-200
7 17,200 6,300 2,760 2,800 1,730 2,20'0 1,320 2,000 1,030 1,600 1,160 1,980
8 13,.700 6,100 2,900 3,600 2,290 2,500 1.,850 2,500 1,590 1,900 1,130 1,200
9 12,700 7,900 2,710 4,800 1,110 2,100. 700 1,280 330 600 180 420
10 18,100 7,400 4,950 5,600 3,770 5,100 3,480 5,100 2,430 3,600 2,290 3,000
11 3,030 2,700 1,780 2,400 1,470 1,700 1,280 2,,000 1,350 2,600 1,170 2,000
12 20,700 8,500 6,550 6,800 4,180 5,300 2,180 4,300 1,840 3,100 1,110 2,400
13 27,900 10,200 1,470 1,800 490 680 200 3JO 52.3 180 42.9 110
14 25,600 11,100 10,400 6,800 534 630 232 370 68*8 130 35.2 45
Porcu-8,610 4,300 2,830 2,800 1,630 2,300 873 1,500 740 1,400 651 1,300
pine
lbte: Tb:· values listed above are average values of the column :IX>rts sampled.
Average values for Porcupine Creek listed under 6 hour. and 12 hour were sampled at 4 and 7 hours, respectively.
'lbtal suspended Solids and Turbidity values for Porcupine Creek after 528 hours (22 days) are 120 ng/1 and
390 mu, respectively.
·---------· • (
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TURBIDITY (T), NTU
A£LA110NSHF BIETWEEN 1\Jft!IDITf .~ND TOTAL SUSPENOID. SOLIDS l
! SETTLING POND DEMONSTRATION PROJECT l
1
2 .s gmr:wsroNS
It was concluded from the turbidity data for the Porcupine Creek settling
column test, as plotted by time on Drawing 3, that reductions in turbidity to
the Alaska standard of 25 NitJ al:::ove natu:r.al conditions could probably not be
obtained in a practical manner by sedimentation alone. Extrapolation of these
data indicated that approximately 60 days of sedimentation would be necessary
to achieve the 25 NTU standard under the laboratory conditions of the test, ..
. ,r~~
assuming negligible turbidit-.t of th~ under na.tural corxlitions.
From this test it was concluded that it would not be practical to design the
demonstration settling pond at Porcupine Creek to achi~ve State standards,
due to the lack of large quantities of clean water for dilution of the pond
effluent and limitations on the size of ·the pond as impos~d by the
dimensional and topograii·lic constraints of the site.
The settling column test data suggest that the settling ponds at the nine
mines with ponds that were surveyed in this study would exhibit an average 85
percent efficiency of removal of suspended sediments. Actual field
measurements of suspended material in the influent and effluent of the ponds
at these sites, however, indicated that an average of only 79.1 percent of
the suspended sediments was removed.. 'lhus, the settling column tests tended
t.o predict, on the average, a substantially better perfoz·mance of the
settling ponds in removing sediments than was actually observed in the field
zreasuranents.
The following are suggested as perhaps the two most likely reasons for the
difference between the field measurements and t.he settling column on test
17
•
results:
1. The samples used in the settling column tests were collected
directly from the discharges of the sluice boxes at the individual
mines. The material entering the settling ponds (which were
usually located from several hundred to several thousand feet
downstream of the sluice boxes) may therefore have differed
somewhat in ~ie distribution of sizes of suspended particles from
the material that was used in the settling column tests. The
possibility of variations of the test sample material from material
of the settling pond influent locations is indicated by large
difference in the total suspended solids concentrations and
turbidity values recorded at the beginning of each settling column
test compared to the total suspended solids and turbidity data
obtained directly from field tests of the infuent to the settling
r:onds.
2. Wind, rainfall, short circuiting of flow through the settling
ponds, convection, and other normal operational factors would be
~cted to reduce the degree of sedimentation that would occur
under field conditions, relative to a more controlled laboratory
enviromnent •
18
SECI'ION 'llmEE
DEM:>NSI'RATION PRQJECI'-IDROJPINE amEK
3 .1 GENEJW, O'BlECl'IVES
The site ?f the demonstration settling pond on Porcupine Creek, designated
in this study as Mine Site 16, is located in the Crooked Creek drainage of
the Circle Mining District, Alaska, as. indicated on Drawing Numbers 1 and 2.
Since the first discovery of gold in 1895 the area has been worked
periodi.cal1;c.. During 1981, three mines were active within the immediate area
of the demonstration settling pond site. Several other mines were operating
downstream from the settling pond on Porcupine Creek or its tributaries.
Many other mines were operating on Crooked Creek and its tributaries during
the 1981 season.
The demonstration settling pond was designed, constructed, and monitored for
the primary purp:>se of providing information with regard to the reduction in
levels of suspended sediments and turbidity that could actually be achieved
under field conditions of typical placer mining operations in Alaska.
Secondary objectives for the demonstration tx>nd study were to evaluate the
effects of settling pond on other water quality parameters, such as pH,
temp:!rature, dissolved oxygen and chemical oxygen denand.
3 .2 FIETD JNYE$TtGs\TIONS
Two field trips were conducted during the 1980 mining sea~on to collect
information for the design of the demonstrative settling pond. The first
trip on July 24, 1980, was a reconnaissance of the site to determine the type
19
of operation, equipnent used, the areas the miner would work the following
season and space available for the settling pond.
The second trip was conducted on August 14, 1980. The purpose of this trip
was to collect information required for the design of the proposed settling
pond and entailed collection of:
1. water quality and flow data from above and below the sluice,
2~ soil samples of the material being sluiced,
3. a water sample fran the oownstream em of the sluice box, and,
4. top:>graphy data in the area downstream from the sluice box and up-
stream from the claim boundacy.
Flow, dissolved oxygen, pi, temperature, and settleable solids were measured
in Porcupine Creek ~;~H-~ mine site and 100 feet downstream from the end
of the sluice box as~ety considerations would allow. Samples for
laboratory· analyses of suspended solids and turbidity were also collected
from the two sample site& The field and laboratory data collected during
this visit are presented in Table 2~t
Samples were collected fran the gold bearing strata in the mine cut and from
the sluice box discharge to define the distribution of the sizes of the
particles of the material being mined and the suspended sediments in the
sluice discharg~. These particle size distributions are shown in Table 13.
A bulk sample of the slui~ box discharge was collected during the· August 14
field investigation for a settling column test (See Section Two).
20
TABLE 2
WATER QUALM DATA CDLLECIED AOOUST 14, 1980
Porcypine Creek Aboye Mining Qperatign
Flow
Dissolved Oxygen
D.O. % Saturation
pH
Temperature
Settleable Solids
Suspended Solids
Turbidity
5.6 cfs
13.0 ng/1
lOS
6.4
8.,0°C
0.1 ml/1 o.a ng,/1
0.20 NlU
Below Sluice Box
Flow *
Dissolved Ozygen
D.O. % Saturation
pH
Temperature
Settleable Solids
Suspended Solids
Turbidity
11.3 cfs
12.6 mg/1
106
6.6
9.6°C
16 ml/1
5910 trg/1
1400 Nro
* Note: Sluioe water was impounded prior to using it in the sluice
Topographic data of the area were also obtained to provide data for the
design of the settling pond and for calculation of the amount of material
that \~ould have to be moved during pond construction.
3 ~3 row DEaiGN
The rate of sedimentation and removal of turbidity that could be obtained in
a settling pond was evaluated in the laboratory, prior to the design of the
demonstration settling pond, by .conttucting a settling test of the collecteQ
sluice box discharge in a settling column. The procedure and results of this
test have been presented in the preceding sect:j.on.
Where waters are used for growth and propagation of aquatic life and
wildlife, ADEC water quality regulations require that tlle turbidity of a
stream not be increased above the background le'Jel by more than 25 NTU as
measured at a point 500 feet downstream from the point of discharge to the
stream. During the design of the settling pond the data presented in Drawing
3 were reviewed to aid in the determination of pond size requirements to
conform with the requirements of the ADEC regulations. These data indicated
that, under laboratory corditions, a settling period of about 60 days would
be required to reduce turbidity levels to 25 NTIJ. Although dilution by the
parent stream and any natural c;:leansing processes within the stream would be
expected to reduce the turbidity of the stream at the point of downstream
measurenent to a lower level than that occurring at the settling pond out-
fall, it seemed unlikely from the settling oolumn data that the proposed site
would penmit construction of a settlL~ pond of sufficient size to meet the
State turbidity standards.
21
The pond was therefore deSigned for the maximum size permitted by the topo-
graphic and claim boundary constraints of the site. From the expected dis-
charge from mining operations it was anticipated that the pond as designed
would provide a detention time of approximately two days. The geometric
configuration of the proposed pond was devt~loped to provide uniform flow
velocities throughout the pond to the maximum practical extent.
The depth of the pond was not considered to be critical in the design;
however, a minimum five foot depth was felt t~' be desirable for storage of
sediment and to limit the effects of wind, rainfall, convection, etc. in
hindering sedimentation. The settling pond design included a filtration
system, consisting of a perforated outlet pi:I;e that was wrapped with a filter
fabric material and buried in the containment dike of the pond. 'lbis provi-
sion was included to allow measurement of any effect of filtering action of
the fill material in reducing the turbidity level and to peritlit evaluation of
the expected reduction in the permeability of the fill during the operation
of the pond.
'1~ settling !X)nd was designed ~ contain only wastettJater from the sluicing
ope!:ation. Strea~'n flows were de~dgned to bypass the settling p:;nd to avoid
interference by stream r1.11ot;f with sEdimEmtation and to limit th(:! I=Qtent:ial
for flood damage.
The outlet from the· settling pond was designed to be a 24 inch diameter
corrugated culvert pipe buried in the earth fill dike that contained the
settling pond. A 24 inch diameter ver:tical standpipe was connected to the
culvert pipe with a fabricated elbow section, Cutoff collars W@I'e provided
22
along the culvert pipe to limit seepage and erosion at the contact face
between the earth fill of the dike and the cW.vert.
The standpife confi9Uration for tbe settling ~oo outlet was includt..~ in thf~
design rather than an overflow weir type {}f outlet. because of the ease of
construction of the standpi~ and culvert systera ana to avoid the potential
problems of erosion associated with overflow weir designs.
It was planned that some alt~rations to the I=Ord ~sign would be ma:de during
the mining season. No specific alterations were planned or studied during
the design phase of the work. The nature of such alterations were to be
determined after evaluating the performance of the pond relative to the
expected results.
Pond construction took place in June, 1981. Because of a change in the
miner's work plan, it was necessary to change the pond location from that
identified in the 1980 field investigation to a new site, approximately 4000
feet downstream. The porx1 design was modified in the field to conform to the
topographic and claim boundary conClitions at the new location.
The pond was constructed using a D-9 Cat dozer. Mine tailings were mixed
with fine grained soils by the dozer to form a relatively impervious core of
the earth fill containment dike. Standard culvert sections were used in
construction of overflow standpipes and the filter culvert. Woven fiberglass
fabric was wrapped around the perforated culvert section to prevent loss of
23
dike material through the culvert perforations. Drawing 6 shows a plan and
profile of the Demonstration Settling Pond, as ronstructed.
Because of the change in pond geometry associated with the revised site
location it was dr..ACided during construction to install two culvert standpipe
f.)utlets rather -than the single outlet that was originally planned.. This
ch(ill~e was made to enhance uniform flow velocities through the pond. The
added GUtlet was constructed of 18 inch diameter culvert pipe.
'l'h~ ~$t of the settling pond construction was $12,000.00. Additional costs
included $5,600,,!;90 for the materials for the standpipes and filter system.
Tbe construction was com~eted in four working days.
A :period of intense rainfall occurred as cx:>nstruction of the I:X>nd was being
completed, with associated high runoff in Porcupine Creek. To avoid flooding
of some equipment in an area that was adjacent to the stream bypass around
the pond, the stream was temporarily diverted through the pond as an
emergency measure during the peak rtmoff. Since only the 18 inch standpi:f.e
outlet had been completed at that time, the pond containment dike was
overtopped by this unexpectedly high flow, washing out a forty foot section
of the containment dike. Repair of this washout, costing $2,200.00 was the
only maintenance that was performed on the dike during the 50 day monitoring
period.
3 .5 MINE OPERATJ:Ot§
'!he miner immediately upstream from the demonstration settling J;X>rxl utilized
24
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DEMONSlMT!ON .SETTUNG POND AND BERM
SECTION A-A
2 -, I I
---"~
FiiNCul.-1
18"0/o.
PORCUPINE CREEK
ClftCLE DISTRICT
SETTLtNI POND OEMON-STR.-noN PfiK>JECT
l DAT. •aAL. Gts Ill-8M" MOo
·~ 12-2-81 NONE LDS * Ol!f04 ~t ___ l---~~.~----------------------'
' '
a trommel (a re-J'ol ving screen app:tl!'atus) to reraove oversized material prior
to slUicingo Water for the sluice and trommel operation was pumped from a
nearby pump pond. The mine, designated in this study· as Mine Site~\~
operated 38 days of the 50 day sampling period. The equipm.ent used in the
operation included one or two dozers piling paydirt, a dragline to load the
hopper which fed the trammel, and either a dozer or front end loader to
remove tailings.
Mine Site 16 operated an average of 7.4 hours on days worked. The hours
worked per day varied from 2 to 11 hours. The average quantity of material
moved was estimated to be between 560 and 700 cubic yards per day. The
absolute range was estimated to be 150 to 1050 cubic yards per day. Between
Days 14 and 15, the sluice and trommel unit was moved upstream approximately
400 feet. At this time the pump pond was r~located upstream. Originally
Porcupine Creek flowed into the pump pond. In the new location upstream, it
was off the stream course with a byt;:ess diverting water from the creek.
The quality of water in Porc~pine Creek at Mine Site 16 was affected by
operations of a mine designated in this study ~'U) Mine Site 15, located
approximately one mile upstream from Mine 16. The miner at Mine Site 15
sluiced during 21 days of the 50 day sampling period.
During high flows water would be routed around Mine Site 15 by means of a
bypass channel. During low flows water was stor~d in a reservoir to be.
released for sluicing.
Porcupine Creek flowed into a containment area formerly used for a water
25
reservoir in a previous mining season, located approximately midway between
Mine 15 and Mine 16. The resultant r.ond allowed some sedimentation of waste-
water from Mine 15 to occur prior to the use of the water at Mine Site 16.
'.ttle mining operations and sampling sites in the vicinity of the demonstration
settling porXi are shown in Draw iJl9 i.
3 • 6 .BJ.W lQllFIC'ATION
Approximately halfway through the 50 day sampling period, various
modifications to .increase pond efficiency were evaluated.
The principal settling pond modifications that were considered included the
installation of baffles and ener.gy dissipater&
Baffles consist of placing curtain walls of plywood or other materials or
gravel berms in the pond to increase the path length of water flow from the
pond inlet to pond outlet. Properly placed baffles can decrease the reach
over which wind can create surface turbulence. 'lbey also help preve.nt short
circuiting. It was decided, however, that it would not be feasible to in-
stall baffles in the pond as a design modification without draining the r:ond
and substantially altering the pond configuration. Further,·gravel berms
would take up a considerable amount of the volume and surface area of the
pond.
'Itle most app;trent effect of the continued mining operations on the pooo, was
the accumulation of sediment at the upper end of the pond. It was therefore
26
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NOTE: 0~&~ ~•
.... Hew u ....
":t .-&-. 1 DA1'. ..ALS .
1
.
g .. 2:5-81 NONE _ :
SITE -I. Above Sluice
2. Daily 8ypou
3. u,_r PcwcupiM Creek
4. hlow Sluice
~. YoHM Creek
6. S.ttl"'t Pond Dam I.Aak
7. Abot11 Peftd
8. Below Pond
9. Pump Pend
10. Below Slul<:e
11. Pond Influent
12. Pond Effluent
A. Confh~Met ~·Pond Efflutnts
B. Ritht Outlet Pipe
C. Lift Outlet Pipe
D. Filter Outl•t Pipe
1~. 500' Downstream
14. By~s
NOTE:
!i&Jice at MiM IS was mo'Mtd 40d .,.. tNt•• doys 14 oftd t5.
S-1• wt.s 9, iO Clfltd 14 were
roloc.tu accordifttly.
Old Pond.
Detnonstroti90
S«tfing Poftd
30,000 ... ft.
56,200 sq. ft.
!J£MONS7RATION
SETTLING PONO
LOS
PORCUPINE CREEK
CIRCLE DfSTRlCT
SETTliNG FOND D£MONSTMTION PROJECT
' I
I
-~---· ------------~------.... ---..;
decided that the pond modification should consist of the installation of a
berm at the entrance to the pond to decrease the inflow water velocity, and
thUS settle out some of the s~nded sediment.
On Day 36 a gravel be.rm was constructed across the pond influent stream,
approximately 60 feet upstream from the p:lnd. The berm was 3' high, 40' wide
at its base and 70' long. See Drawing No. 8. This created a small settling
pond with an area of approximately 10,000 square feet. The cost of this
modification was $400.00.
3 • 7 DATA QJI.I.Eljl'ION
The water quality sampling program included 14 sampling sites with 8 sites
sampled once daily, four sites (designated as Sites 10-13) sampled twice
dail~ :md two sites (designated as Sites 3 and 5) sampled periodically.
Daily sampling at the two mines concentrated on the days that they were
operating. Drawing 7 shows the location of the 14 sample sites. The sample
sites are described in Appendix II.
The following parameters were collected at each sample site:
Dissolved Oxygen
Water 'l'emperature
Air Temperature
pH
Settleable SOlids
Flow
Total Suspended Solids
Turbidity
Chemical oxygen demand wa~i .sampled during high and medium flows. Arsenic was
sampled onc;:e durir..g the 50 c.tay sample period at the following three loca-
tions:
27
San1ple Site No. 1 (Above Sluice t2), Mine 15
sample Site No. 11 (At Pond Influent) , Mine 16
Sample Site No. 12A (At Confluence of Pond Effluent), Mine 16
The method of collection of water quality ~ples is described in Appendix
II.
Field data collected over t.he 50 day sampling period are presented in
Appendix III.
3.8 BESQLTS
Surrmacy ,gf Data
Mine 16, whose discharge was received by the demonstration settling ~nd, did
not utilize water in its natural condition for its sluicing operations, due
to the effect of upstream mining operations, principally Mine 15.
The means, standard deviations and ranges of water quality data collected
upstream from Mine 16 are presented in Table 3. Data collected \qhile Mine 15
was operating is tabulated separately from data collected while Mine 15 was
not OI;:erating.
The means; standard deviations and ranges of water quality data collected
from the demonstration settling pond and Mine 16 sampling stations are
presented in Table 4. Data collected while Mine 16 was operating is
tabulated separately from data tha.t was collected during periods when Mine 16
was not operating.
28
TABLE 3
WATER QUALITY mTA FRCt-1 SAMPLIN:i SITES IDCA'reD
UPSTRFAM OF MINE 16
While Mine 15 While Mine 15
.waa~ ~ .Nat Operating
SamPling N Mean Standard Range N Mean Standard Range
Site~. Deviation Deviation
AIB .mMPERATURE • ~
1 Above Sluice 25 13 6 2-23 20 13 5 1.,.24
2 Daily BypaSS 8 10 6 2-20 12 12 5 0<-16
4 Below Sluice 20 13 6 2-23 Not Sampled
7 f;bcNe Pond 5 7 2 3-9 2 5 5 1-8
8 Below Pooo 5 6 3 1-9 2 6 4 3-8
DISS)LVED QXYGEN, uw'l
1 N:Jove Sluice 25 11.3 1.1 8 .. 5-13.3 20 11.8 0 .. 8 10.4-13.2
2 Daily Bypass 9 10.7 1.5 8 .. 0-13.3 12 11 .. 0 0.98 10.3-12.8
4 Below Sluice 20 11.5 1.4 8.1-13.5 Not Sampled
7 Pbove Pond 5 10.0 2 .. 0 8.3-13.0 2 10.7 2.1 9.2-12.2
8 Below Pond 5 10.1 1.2 9.1-11 .. 7 2 11.4 1.4 10.4-12.4
WATER~~
1 Above Sluice 25 8 2 1-12 19 8 2 5-11
2 Daily Bypass 9 7 4 1-12 11 10 1 8-11
4 Bela\': Sluice 20 8 3 1-12 Not Sampled
7 N:x:Ne Pond 5 5 2 1-7 1 6
8 Below Pond 5 5 3 Ooc•8 1 8
liiL. iii UNITS
1 Above Sluice 21 6.7 0.2 6.1-7.1 11 6 .. 6 0.2 6.3-6.9
2 Daily Bypass 7 6.5 0.3 6.0-7.1 1 6.3
4 Belor.N Sluice 17 6.5 0.3 6.0-7.0 Not Sampled
7 Above Pond 6 6.6 0.3 6.0-6.9 4 6.4 0.2 6.1-6.5
8 Below Pond 6 6.5 0 .. 3 6.0-6.9 4 6.4 0.2 6 .. 1-6.6
SETI'I JWY.E SOLIDS, ml/1
1 Above Sluice 26 Oe7 1.3 0.0-2.5 24 0.7 1.0 0-4.1
2 Daily Bypass 10 0.2 0.6 0 .. 0-2.0 12 0.2 0.5 0-1.8
4 Below Sluice 21 22.1 8.7 5 .. 5-32.0 Not sampled
7 'PJ.x:Ne Pond 6 4.4 2.8 0.4-8.0 4 0.6 0.5 0.1-1.,0
8 Below Pood 6 0.8 0.6 0.2-1.5 4 0.3 0.4 o-o.a
FUM • .W
1 Alx>ve Sluice 23 10 8.3 2-34 20 15 .. 4 16.,2 3.4-58
2 Daily Bypass a 9.8 7.2 0.8··"18 11 3.2 1.4 1.5-6.0
4 Below Sluice 19 11.1 1.2 1.2-13 Not sampled
7 Above Pond 1 26 1 35
8 Below Pond 1 21 1 37
SaJl1?ling N Mean
Site No.
'IUPBIDir!a mY
1 Above Sluice 26 330
2 Daily Bypass 10 29
4 Below Sluice 21 3366
7 Above 1\ond 6 789
8 Below Pond 6 645
.mt. ~~.m mr,mc;;, m/1
I }bove Sluice 26 449
2 Daily Bypass 10 29
4 Below Sluice 21 6516
7 Above Pond 6 844
8 Below Pond 6 502
qiEMICAL QX¥GEN DOON) •. ~~-
1 Above Sluice 1 51
2 Daily Bypass 1 67
4 Below Sluice 1 270
7 Above Pond 1 97
8 Below Pond 1 ~'F'"
l""" ...... ~
TABLE 3
(a::m'IWED)
While Mine 15
liaa cpratJ.rs
Standard Range
Deviation
444 3.2-1600
26 6-80
1765 1500-7200
652 31-2000
252 170-900
599 1.5-2070
26 2.2-74
4728 1770-22200
835 16.5-2440
244 171-805
While Mine 15
Baa &t Operating
N Mean Standard Range
Deviation
24 468 616 1.8-2200
12 187 171 6-500
Not Sampled
4 1499 2868 30-5800
4 172 162 32-400
24 608 884 0.1-3770
12 4r17 401 5.6-1310
Not Sampled
4 203 3579 95-7390
4 115 98 36-240
49
TABLE 4
WATER (JJALI'lY 1l1\'m FROM MINE 16 SAMPLIR; srrrES
While Mine 16 While Mine 16
BAa '"rating ~ lQt e&eratjm
N Mean Standard Range N Mean Standard Range
sampling Deviation Deviation
Site No.
AlB IFJWfUWIVRE' ~ 29 13 6 2-25 6 14 7 3-22
14 sypass 32 13 5 6-25 6 14 9 3-22
9 Plll1P Pond 52 14 .. 6-25 Not Sampled Bel~ Trorrmel :>
10 Pond Influent 60 13 6 1-24 17 14 5 3-21
11 Pond Effluent 43 14 5 2-23 15 14 5 3-22 12 Filter OUtlet 12 13 5 2-20 3 12 7 •1-18 12D PoJXi Dan Leak 16 14 4 6-20 8 14 3 11-18 6 soo' oownstream 60 13 5 2-23 18 14 5 3-22 13
i>I®LVED OXYGEN, m»/1
14 BypaSS 29 11.4 1.0 9.3-13.4 6 12.1 0.7 11~2-12.09
9 PllnP Pond 32 10.8 1.1 8.5-13.5 6 11.0 0.9 9.4-11.7
10 Below Trammel 53 11.6 1.0 8 .. 5-13.3 Not Sampled
11 Pond Influent 61 11.0 1.0 8.6-13a5 18 10.8 1.0 9.2-12.5
12 Pond Effluent 44 11.7 0.7 10.2-13.1 15 11.3 0.9 9.5-12.8
120 Filter OUtlet 12 10.8 0.8 9.7-12.1 3 10.5 1.3 9 .. 5-12.0
6 Pond Dan Leak 16 10 .. 8 0.6 9.7-12.1 8 10.2 0.7 9.1-11.1
13 500 • Downstream 62 11.1 1.1 8.6-12.6 18 11.0 0.9 9.3-12.5
WATER .TF.MPERATPRE' ~
14 BypaSS 29 9 3 2-14 5 11 2 8-12
9 PlJnp Pond 32 10 2 6-14 4 11 1.0 7-12
10 Below Trcmnel 53 10 6 6-14 Not .Sampled
11 Pond Influent 61 9 3 1-13 16 11 2 8-15
12 Pond Effluent 44 11 7 2-14 13 11 2 9-14
120 Filter OUtlet 12 9 3 1-11 3 11 1 10-12
6 Pond Dam Leak 17 11 1 8-13 8 11 2 6-13
13 soo' Downstream 61 10 2 2-18 16 l2 2 9-14
~. J;ii UNITS
14 Bypass 19 6.6 0.2 6.1-7 c;o 2 6.2 0.2 6.0-6.3
9 Ptmlp Pond 23 6.6 0.2 6.2-7.0 2 6.2 0.1 6 .. 1-6.3
10 Below Trcmnel 38 6.3 0.4 5.4-7.4 Not Sampled
11 Pond Influent 42 6.2 0.3 5.2-6.7 10 6.0 0.3 5.5-6.3
12 Pond Effluent 31 6.3 0.3 5.6-6.8 9 6 .. 0 o.s 5.1-t;.5
120 Filter Outlet 6 5~8 0.4 5.3-6.5 1 6.J.
6 Pond Dan Leak 6 6.4 0.2 6~0-6.6 4 6.2 0.1 6.1-6.4.
13 500 • Downstream 42 6.3 0.3 5.5-6.8 10 6~~1 0.4 5.4-6.3
Sampling N Mean
Site ~.
Sttl"l't.E'.M~ SQI.IDS, ml/1
14 Bypass 34 2.5
9 P\Jnp 1:\!>nd 37 0.2
10 Below Tramel 62 51
11 Pond Influent 70 12.1
12 Pond Effluent 51 o.s
12D Filter Outlet 15 0.6
6 Pond Dam Leak 18 1 .. 3
13 500 • Downstream 71 Oo4
fUM, .w
14 Bypass 23 11
9 Pllnp Pond
10 Below Trarmel 60 7 4 ' .
11 Pond Influent 65 8.2
12 Pond Effluent 52 6.3
12D Filter OUtlet 19 0.1
6 Pond Dam Leak 18 0.02
13 500' Downstream 54 5 .. 3
WRBIQITY I .mu
14 Bypass 33 560
9 Pt.rnp Pond 37 477
10 Below Trcmrel 62 6531
11 Pond Influent 70 2989
12 Pond Effluent 51 1807
12D Filter Outlet 15 2273
6 Pond Dam Leak 14 1593
13 500' Downstream 71 1616
r;rorAL SUSPEWED SOLIDS 1 ug/1
14 Bypass 34 1366
9 Plnp Pond 37 486
10 Below Trcmoel 6215450
11 Pond Influent 70 4212
12 Pond Effluent 51 1397
120 Filter Outlet 15 1746
6 Pond Dan Leak 13 1832
13 500 • Downstream 71 1284
i.
TABLE 4
(a:Nr!WED)
While Mine 16
.WSW cprating
Stand':lrd Range
Deviation
3.8 0.0-17 o.s Oo0_,2.8
34 0.2-130
10.8 0.0-48
0.4 0.0-1.5
0.7 0 .. 0-1.5
1.8 0.0-i .o
0.4 Oa0-2.0
14 0.2-60
2.0 5.6-7.8
2.7 0.5-13
5 .. 3 0.9-37.1
.03 o .. o-o.1
.04 o.o-o .. 1
2.8 0.9-11
556 70-2400
322 45-1600
4016 180-15000
1838 110-8000
857 45-4600
1729 650-7500
623 180-2900
883 650-5400
3441 44-19700
533 44-2780
14000 160-59800
3202 155-16500
711 285-2540
2254 180-9380
1082 370-4600
738 200-4560
N
6
6
17
15
1
8
18
5
16
17
7
7
15
6
6
18
14
3
7
18
6
6
18
14
3
8
18
While Mine 16
lYaa ~ Qperating
Mean Standard Range
Deviation
1.7 1.4 0.0-3.7
0.2 0.4 0.0-1.0
~t Sampled
0.8 1.8 0.0-7.5
0.1 0.1 o.o-o.2
0.1 0.1
0 .. 4 0.1 0.0-0.3
0.1 0.4 0.0-1.0
4.5 1 .. 7 1.8-6~0
Not Sampled
2.9 4.1 0.4-18
2 .. 3 3 .. 3 0 .. 2-15
O:Jl 0.04 0.0-0.1
0.1 0.2 o.o-o.s
2.2 3.6 0.3-15
380 351 60-1000
243 226 100-700
Not Sampled
224 274 20-900
443 254 45-800
410 135 280-550
503 437 140-1400
602 781 50-3500
514 468 104-1410
572 709 96-1990
ax Sampled
402 440 13-1550
1124 2686 26-1070
455 169 345-600
582 214 215-920
509 308 40-1100
While Mine 16 While Mine 16
Baa ~rating ~ lilt <&erating
N Mean Standard Range N Mean S~ndard Rang a
~lin9 Deviation Daviation
site ttl.
SJffiMICAL .QXYGfiN PEMANl· ng/l
sypass 2 54 54.5 15-92
14 1 26
9 PU\1P Pond 1 620 -10 BelOW Tratmel 3 119 52.5 89-180 Pond Influent ....
11 2 72· 19.1 58-85
12 POD:3 Effluent
1 100 Filter OUtlet ...
120
6 POnd r.an r..e3k
2 8~ 38.2 55-110 500 • !')oWJ'lstream v-
13
fAT~ te.t amli~ BJttlral .u.ua ... _ -
_,.,~,ity upstream of Mine 15 uas affected by the discharge of a small
water \:.i~
. ne that began op!rations on Day 21. Data collected from sample site
placer nu.
. to Day 21 represented the "natural" water quality of Po~;cupine Creek. 1 pr1or
mk following tabulation presents water quality data for Porcupine Creek in
:.u .. e
its natural condition~ and at Sampling Site 8, between Mines 15 and 16.
'lllese dat-.a at·e compared to water quality values ootained from the discharge
of Mine 16 {wh.ile operating) at Sampling Site 10, immediately below the
trommel and sluice:
Water Temperature°C
PI
Dissolved ~..<.ygen 1D3/l
Total Suspended
Solids mg/1
Turbidity 1.\"'IU
Setteable Solids ml/1
ChEmical Oxygen
Demand mq/1
Sample Site 1 Sample Site 8 Sample Site 10
Above Mine 15 Between Mines 15 & 16 Below Tramnel
Mine 15 Mine 15 Mine 16
{Days 1-20) Working Not Working O};erating
6.9 5 8 10
6.6 6.5 6.4 6.3
11.0 10.1 11.4 11.6
13 .. 2 502 115 15,450
8.6 645 172 6,531
0.03 o.a 0.3 51
15 65 620
As indicated in the above tabulatioo, the levels of settleable solids, total
suspended solids, turbidity, and chanical oxygen demand, as measured below
the trommel and sluice, differ from values of the waters of Porcupine Creek
as measured between Mines 15 and 16 by more tl'um one order of magnitude. For
this reason the efficiency of the demonstration settling pond in removing
29
suspended and settlable solids and chemical oxygen demand was not considered
to be affected by the noted differences in the quality of water received from
Porcupine Creek, compared to natural conditions.
Pond .fi<zw Measurements
Flows from the p:>nd were measured at four locations, i.e. at each of the two
pond outfall pipes (sampling sites 12B and 12C "Pond Effluentn) at the outlet
of the perforated pipe wrapped in filter cloth that was buried in the
upstream side of the containment of the pond (sampling site 120, "~"'ilt~r
OUtlet") and at a small leak through the fill of the con~ent dam~ (Sample
I
Site 6, "Pond Dam Leak"). As indicated in Table 3, the flows at these latter _
two locations were negligible compared with the pond effluent for the two
outfall pipes.
When the trammel and sluice at Mine 16 were not operating, an average flow
into the pond of 2.9 cfs was still recorded, due to surface and groundwater
inflow between the pump pond and the tailrace ..
.Eff~ ~ Mine e&eralions
When Mine 16 was not operating the mean levels of total suspended solids,
settleable solids and turbidi~ at the pond influent were only 10, 7, and 8
percent, respectively, of the meanlevels that were measured at the pond
influent while the mine was working. Dissolved oxygen, pH and water
tem:perature data did not show appreciable change at the pond influent between
operating and non-operating cases.
30
suspended and settlable solids and chemical oxygen demand was not considered
to be affected by the noted differences in the quality of water received from
Porcupine Creek, compared to natural conditions.
Pond Flow Measurement:;
Flows from the p:>nd were measured at four locations, i.e. at each of the two
pond outfall pipes (sampling sites 12B and l2C "Pond Effluent") at the outlet
of the perforated pipe wrapped in filter cloth that was buried in the
upstream side of the containment of the pond (sampling site 12D, "Filter
Outlet") and at a small leak through the fill of the con~ent dam~ (Sample
I
Site 6, "Pond Dam Leak"). As indicated in '!'"able 3, the flows at these latter.
two locations were negligible compared with the pond effluent for the two
outfall pipes.
When the trommel and sluice at Mine 16 were not operating, an average flow
into the pond of 2 .. 9 cfs was still recorded, due to surface and groundwater
inflOW' between the pump pond and the tailrace$
Effect .Qf M;Lne Ogerations
When Mine 16 was not operating the mean levels of total suspended solids,
settleable solids and turbidity at the p::>nd influent were only 10, 7, and 8
percent, res:pectively, of the meanlevels that were measured at the pond
influent while the mine was working. Dissolved oxygen, pH and water
temperature data did not show appreciable change at the pond influent between
operating and non-o~rating cases.
30
h mine was not working, an increase in the turbidity and total
when t e
ded solids was noted across the pond, from 224 to 443 N'IU, ana from 402
susp:!Il
to 1124 mg/1 resp!ctively w 'lbe reason for this increase is unknowno
_Effgctiveness .Qf. Tailrace .and Pond
The tailrace between the trommel and the pond influent was about 250' long
during the first 2 weeks of sampling and about 650 1 long during the last 5
weeks of ~pling. The mean levels of settleable solids and total suspended
solids were reduced by about. 75 peJ:cent in the tailrace, and mean turbidity
level at the pord influent was reduced to ab:.>ut half a-te level measured below
~ trommel. Comparison of the pr;nd effluent to the influent indicates that
the percentage removal of mean settleable solids, total suspended solids, and
turbidity was 97 percent, 60 percent, and 38 percent, respectively.
Temperature, til and dissc1ved oxygen exhibited no significant change across
the pond. The chemical oxygen demand decreased from 119 mg/1 at the influent
to 72 mg,/1 at the effluent.
The average 60 percP-nt removal of total suspended solids measured across the
pond compared with a predicted 87.4 percent removal as predicted by the
settling column test of material obtained from the sluice discharge at
Porcupine Creek. Application of Stoke's Law of settling velocities in a
fluid indicates that a removal efficiency of 78 J;ercent would be attained.
(See more detailed discussion in Section Fpur)
Comparison of the levels of turbidity, total suspended solids and settleable
e;olids in the pond effluent to the percentage of the pond volume that was
31
occuppied by sediments indicated little or no correlation between these
parameters. Water quality at the 500 1 downstream sample location was similar
to the pond effluen~ However, the mean turbidity and TSS levels displayed
slight increases over the pond effluent levels, probably due to erosion of
exposed surface soils in the outfall channel.
Because sampling 500 ft. below the point of discharge into the receiving
stream (Porcupine Creek) was impractical, and because the creek water quality
was itself influenced by the activity of f.1ine 15, water quality at a poing
500 feet downstream of the p:>nd effluent at Mine 15 was used to approximate
the conditions for compliance with the State Standard.
The mean levels of total suspmded solids, dissolved oxygen, temperature and
pH of the pond effluent, as measured 500 feet downstream of the pond while
Mine 16 was operating, were within ten percent of the mean values of these
parameters as measured in Porcupine Creek at Sapling Station 14, in the creek
bypass around fo\ine 16.
Settleable solids at the 500 foot downstream location averaged 0.4 ml/1
compared with a average of 2.5 ml/1 at Sampling Station 14o Although mean
levels of total suspended solids at the 500 foot downstream location were
~ightly lower than in the Porcupine Creek BypaSS, the mean turbidity levels
were swstantially higher, averaging 1616 NlU while the mine was operating,
compared with 560 NTU in the bypass. Chemical oxygen demand in the bypass
averaged 54 mg/l compared with an a'verage of 83 mg/1 in the pond effluent
measured 500 feet downstream of the outfall.
32
d effluent measured 500 feet downstream, the minimum State
'l'he pon
. nts for dissolved oxygen concentrations of 7 mg/1 in all cases. requ 1 reme
t mperature exceeded the 13°C standard on five occasions, all between water e
JulY 20 and July 27. On four of these occasions temperatures of 14 °C were
ed with l8°C measured once. measur ,
The pH level, measured 500 feet below the pond discharged was less than 0.5
pH units from the pH value measured above the sluice in 36 of 54
measurements.
water samples for total and dissolved arsenic analyses were collected at
three locations on one occasion. Results of these analyses, in mg/1, are
presented below.
~ LDcation
per..ne Sluice (1)
Pond Influent (11)
Pond Effluent (12)
Disso1ved Arsenic
0.0012
0.0042
0.0045
SU§Pellded Arsenic
0.0015
1.026
0.166
The conca~trations of both fractions of ar$enic increase below the sluice at
Mine 15 and the suspended fraction has higher concentratons than the
disJolved fraction. Dissolved arsenic concentrations remained essentially
unchanged between the pond influent and effluent, but suspended arsenic
oocreased by about 84 percent in the pond.
Drawing 8 shows the concentration of settleable solids at the pond influent
and p:>nd effluent before cu"'ld after placement of the berm. Immediately after
•
33
DA,.a
11-23-lf
20
ll
It
......
i 14
!
-t2 5
fA
LU 10 ..J
2
I.AJ
~ 8 .....
~
4
2
HJitM ADD£0 --.J
.e.AL8
AS SHOMI
POND
INFL.UIWT
• aM ODNIIU&.TANTti,INC·
,..POND
EFP't.U£NT
48 ..
TROMMEL DOWN
EFFECT OF BERM PLACEMEN1
ON SETTLEABLE SOLI OS
SETTLING POND DEMONSTRATION PROJECT
·c:n•e11-•v 11.....,8CT NO. a.AWINa NC
WA 013104 8
. -·---------------
placement of the berm the settleable solids in the pond influent were reduced
by 95%. Between Day 37 and 38 total suspended solids decreased by 86% and
turbidity decreased by 77% at the J.X>OO influent. Within 10 days settleable
solids had increased to 32% of the pre-berm value and showed continual
increase.
The following conclusions can be drawn from the study of demonstration
settling pond:
1. sedimentation Effectiveness
The efficiency of the settl~ pond in removin1 suspended ~diments
was substantially leas than the prediction developed from the
settling column test, as well as the removal efficiency calculated
from Stoke's Law. 'Ibis lower effieiency is believed to be largely
due to the less favorable conditions for sedimentation in a field
environment in canparison to controlled laboratory conditions.
' . . ~-JVZ~t'"~ o...e-v Turbidity levels of the pond effluent at the outfall, oner aging
1593 NTU, was sllbstantially higher than the State standard of 25
Nru above natural levels, measured at a point 500 feet downstream
from the point .of discharge into the receiving stream.
The pond was generally ~~fective in limiting settleable solids to
State standards of 0.2 ml/1 ,above natural oonditions, with 56 of 89
measurements meeting this standard.
34
•
4.1 GfiNEBAL
SECT!OO FOUR
INDIVIDUAL MINE SURVEY
Fourteen placer mines,in the Fairbanks and Circle mining districts (in
addition to the two on Porcupine Creek) were surveyed to gather
representative information regarding the effectiveness of settling ponds and
information on water use. The Alaska Department of Conservation selected
sites based on geographic location, access, and willingness of the miner to
participate in the study. The mines were selected both with and without
sediment control and with varying types of sluices an~ water use for
comparative purposes. Table 5 lists the 16 mine sites, the creeks they are
on and the numbers that have been assigned to the mines for reference
purposes in presenting the data. These locations are also shown in Drawings
1 and 2.
4 .2 OP.JECI'IVES
The fourteen mine sites (in addition to the two at Porcupine Creek) were
selected for study in res};Onse to public comment regarding conclusions that
might be reached in studying only a single site, given the high degree of
variability from site to site in terms of the material worked, methods of
working, topographic or other constraints and natural conditions of water
quality. 'Ihese comments reflected a general concern that the results of the
studies of the demonstration settling pond might not be applicable to other
creeks or mining districts.
37
..
TABLE 5
SE,..l'It.rm PCH> DEltDBl'RATICE PRlJEcr
MINE SITE LOCATIONS
f1ining Site Nunjler Creek Mining· Pistrict
1 Fish Fairbanl\s
2 Fairbanks Fairbanks
3 Gilmore Fairbanks
4 Fagle Circle
5 Eagle Circle
6 Faith Circle
7 Mastodon Circle
8 Miller Circle
9 Mastodon Circle
10 Manmoth
·;
Circle
11 Crooked Circle
12 Deadwood Circle
13 Chena River Fairbanks
14 Fllllle Fairbanks
15 Porcupine Circle
16 Porcupine Circle
The study of sedimentation at these additional mine sites was designed to
allow a more general application and interpretation of the re.sul ts of the
intensive study of the demonstration settling pooo, and to further define the
relative efficiencies of various mining methods for achieving State and
Federal water quality standards.
4. 3 Mimi QEERATIONS
Table 6 summarizes the mining equipment used, method of classifying paydirt,
methods of processing paydirt, number of ponds used, if any, and whether the
mine operates instream or not. A mine is classified instream if the stream
is routed through the settling pond. For mines without ponds, it is
classified as instrearo if the sluice box is fed directly by the stream or if
the sluice oox empties directly into the receiving stream.
n>zers were the predominant earth moving equi.t:'ruQ1t used. W!'i le ~ery mine
had at least one dozer, seven mines had two or more. Eight of the sixteen
mines used dozers to load the sluice box, five used them to strip overburden,
two used them to remove tailings from below the sluice box and one mine used_
a dozen for miscellaneous work. Thirteen of 16 mines used a front end
loader. Five mines used two or more. Tailings were removed by front end
loaders at nine of the thirteen mines. Five used them to load the sluice box
and one used a frontend loader to feed the dragline. Three of the five mines
using draglines used them to feed the sluice box or trommel. The remainin3
two mines used draglines to remove tailings from below the sluice box. A
hydraulic giant was used at only one of the mines studied. Six of the
sixteen miners used single channel sluice boxes ·while one used a double
38
TABLE 6
BJUIPMENr AT SELEcrED PLACER MINE SITES
MINE SI'm i PORQ]piNE .cR..
Jl. Jl J5. .tit J2 J.8. .D JlO. .Ill ID. .Ill Jl.4. .115. .11§.
EQuignent Used
Dozer 1 1 2 2 1 2; 1 1 2 1 2 1 2 1 1 4
Loader 1 1 0 0 1 2. 2 1 3 3 1 2 1 0 1 1
Conveyor 0 1 0 0 0 ()4 0 0 0 0 0 0 1 0 0 0
Drag1ine 1 1 1 1 0 0 0 0 0 0 0 0 Cl 0 0 1
Backhoe 0 0 0 0 0 (l 0 0 1 0 1 0 1 0 0 0
Giant 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
Pump 1 4 1 1 1 1 1 1 1 1 1 1 1 2 1 2
Sluice Box 1 1 3 3 3 3. 1 2 1 5 3 1 3 3 1 3
(nlllltJer of
channels)
Trommel N N N N N N N N N N N N y N N y
Stationary N N N N N :c N N N N N N N N N N
Screen
Vibrating N N N N N N y N y N N y y N N N
Screen
Recycle N y y N N N N y y N N N N y N N
Settling 6 3 3 0 0 1 0 1 1 0 0 0 3 1 1 1
Pond (&:>.
of Ponds)
Instream N y y N N N N y N N N N N y y N
R>te: Numbers indicate the quantities of items at each site. Y or N indicate Yes the miner has that piece of
equipnent or No they do not.
channel, eight used a triple channel and one used a five channel sluiee oox.
Methods of material classification included stationary screens (grizzlies),
vibrating screens, and revolving screens {tromrnels). Of the t'A'O miners using
trommels, one used it in conjunction with a. conveyor and vibrating screen.
The other used a hopper, without a screen, to feed the trommel. Vibrating
screens were used at four ()f the five other mines using screens.
Table 7 shows ranges of piydirt sluiced ·per bou.r and hours worked by the 16
mines that were surveyed in this study. The avf:rage range of paydirt moved
was 95-130 cubic yards per hour sluicing.. These sixteen operations averaged
9 hours sluicing on days sampled.
For purposes of comparison, multiple p>oos were grouJ;.ed with single ponds.
Only one of the four mines with multiple ponds was sampled between ponds.
(See Mine Site #3). Mine Sites 1, 2~ 3, and 13 had multiple s~ttling ponds
in series, while mine sites 6, 8, 9, 14,15 and 16 each had a single settling
pord. The remaining S\ites did not have ponds.
Mine Sites 1 and 2 had ponds which were only being utilized on the first
monitoring trip, and only on trip 3 to Mine 8 was the I;Orrl at this site beirx}
used. Tables utilizing this data are annotated accordingly.
Surface loading, as indicated in Table 8, is a measure of the flow rate from
the pond per Wlit surface area of the p:md. Mine sites il and 19 had surface
loading values signficantly larger than the remaining eight mines with
settling tonds, i.e., the flow rates through the settling ponds at these two
· sites, relative to pond surface area, is significantly larger than at the
39
TABLE 7
SUI91ARY OF MINE OPERATIONS
Water
Material Required Water Use
~ Type of Material ~ved, Hours to Sluice Gal/min
site creek Processing Yd./Hour Worked One Cu.Yd. Sluicing
I
Fish Elevated Sluice Box, Gia'lt 75-100 8 Not Avail. 3680*
l FairbankS Dragline Loading Sluice Box 25 9 1600 280
2 cat J..oadinq Sluice Box 90-100 8 1900-2100 3100
3 GilJnOre cat Loading Sluice Box 90-100 9 1800-2000 3000
4 Eagle Cat Loadii'l9 Sluice Box 80-100 2/lOhr 2900-3700 4900
5 Eagle Shifts
r<1a,th Sluice Box with Grizzly 175 11 1300 3800
6 . ... Vibrating Screen Conveyor 60 11 300 300
i MaStodon cat Loading Sluice Box 150-200 8 1500-2000 1886
8 Miller
Mastodon Vibrating Screens 150 8 560(E) 1800
9 80% Recycle
10 MarrmOth Loader Feeding Sluice Box 150-170 8 1200-1300 3300
erooked cat Loading Sluice Box 150-200 8 1200-2000 4500 11 oeadwood· Loader Feeding Washing Bin 60-80 8 2900-3900 3900 12
13 Qlena Vibrating Screen to Con-150-200 8 390-520 1300
veyor to Trarrne1
14 FltJDe cat Loading Sluice Box 40-50 10 2600~3300 2200
80% Recycle
15 Porcupine
Sluice 2
cat Loading Sluice Box 90-115 8 .. 3 2700-3500 5400
16 Porcupine Tronrne1 75-100 7.4 2000-2500 3300
Sluice 1
'12\BLE 8
WA'JER USE 1\R) ~~sE=-n•rnw11JIR2 RH> CIJARACl'ERISTICS
MINE WA'lER FiltlRATE FU.liRM'E JniD ARFA KIID SJRFl\CE RliD OVEmUJi
SI'JE USE WHm INIO J.QI) FlO! RH> (ACRES) VOUJE IllADIR2 DETENI'IOO VErDCl'lY
SLUICIN3 mm mm ArnE-Fr WHILE Tlfa!E WHILE. nuv'aec xl0-3
GAl/MIN SUJICIH; SllJICIK; SWICIR2 SLUICI~
GM/MIN GAI/MIN :rNFUli (IDJRS)
G.P.M. ACRE
1 3680* 4490* 2870* 0.31* 1.6 14,500* 2 225*
2 280 270* 404* 0.37* 1.5 750* 30 12*
3 3100 3100 2000 2.57 18.0 1,200 32 19
4 3000 ""'
5 4900 ,_
6 3800 6733 3500 4.25 8.6 1600 7 25
7 300
8 1886 1886** 2100** 0.49** 2 .. 0 3850** 6 60**
9 1800 1886 1500 0.08 0.2 23,500 0.6 364
10 3300
11 4500
12 3900
13 1300 1436 1500 1.89 7.6 760 29 12
14 2200 1661 490 0.48 1 .. 9 3460 6 54
15 5000
16 3300 3667 2830 1.29 3.36 2840 5 44
* TRIP 1 ONLY
** 'IRIP 3 OOLY
... ~,en mines with ponds. other J:l'liii"
The overflow velocity indicated in Table 8 is determined by dimensional
conversion of the surface loading. According to sedimen·tation theory1 for
. dirnentation to occur within the pooo, soil particles must be large enough se
to have a downward settling velocity that is equal to, or greater, than the
overflow velocity. Smaller particles (that settle at a lower rate of
velocity) will pass through the pond and remain as suspended sediments within
the f.Oil.i effluent.
sampling started June 11th and finished Se~tember 15th. Each site was
sampled on three different days, allow ... :lg data to be ootained Wlder different
creek flow conditions. For those mine sites having settling ponds, the
following minimum locations were sampled: the miner's water source or pump
pond; below the sluice box; the pond influent; the pond effluent; and 500'
downstream in the receiving stream from the point of discharge of the mining
oteration into the stream. Mine sites without ~nds were sampled at t."'lese
minimum locations: at the water source or pump pond1 below the sluice box; at
the end of the tailrace or bypass; and 500' downstream of the point of
discharge of the tailrace into the main stream.
Water quality tests were the same as previously described for Porcupine Creek
except that C.O.D. tests were not conducted and arsenic was sam~led only in
the pump pond and at the pond effluent or end of tailrace. 'rhe method of
collection and analysis ·of water quality samples was the same as for
40
Porcupine Creek. See Appendix II for descriptions of methods used.
IOOividual mine site maps, descriptions of method of operation and sununary of
field data are presented in Appendix rv.
Bulk (60 gallon) water samples were collected at a point 10-30 feet below the
sluice bo~ at each mine site. Paydirt was collected from the mine cut at
each site. Settling column tests and particle size analyses were conducted
on this material. The results of the settling column tests have been
discussed in Section TWo.
Particle size analyses were run on the paydirt using ASTM Test Procedure
D422~
Flows were determined by use of a staff-mounted pigmy current meter to
determine current velocities across the cross section of the stream. These
velocities were integrated with the depths and incremental widths of flow
across the stream to define the total stream discharge.
To compute the hydraulic flow parameters of the sluice boxes at each mine the
slope of the sluice boxes were measured with a clinometer the depth of flow
in the sluice box was determined by averaging measurement between and over
the riffles.
Since flow measurement could not be taken in side channels of sluice boxes
the flow was assumed to be divided equally in each channel. Flow
measurements used in these calculations were measured 20-40 feet downstream
of the sluice box.
41
4 .5 BEffilLTS
t ural water condition could be determined ty the quality water from
The na
les taken at the above sluice location was at those mine sites where samP ·
other upstream mining operations or disturbances did not affected the
upstream water quality. Data from mine sites tl, 2, 3, 6, 8, 13 and 14 were
~ to compile the above sluice data presented in Table 9, representing the
natural water quality. Sample Site 1 between days 1-20 was used for the
natural quality of Porcupine Creek.
oissol ved oxyg~n levels and the natural percentage saturation of dissolved
oxygen as measured in the above sluice sampling locations, were relatively
high, which is typical in clear upland, streams of interior Alaska. It should
be noted, however, that the high end of the range for percent saturation,
111, is unusually high. The next highest percent saturation was 105. The
is close t(."' being typical, but it is uncommon to measure pH values as low as
6.0, the low end of the measured range. The next highest pH value was 6.1,
and a range from 6.5 to 7.7 would be more typical. Settleable solids were
consistently 0.1 ml/1 or less, which is characteristic of undisturbed, clear
water streams in interior Alaska. The Above Sluice ranges for total
suspended solids (TSS) and turbidity were somewhat wider than expected for
natural conditions. The highest TSS concentration, 67 mg/1, was followed by
concentrations of 40, 32, 28, and 25 mg/1, and the four highest turbidity
levels were 55, 50, 45, and 26 NTU. Also, ·the standard deviation for these
parameters indicates a large amount of variability. Therefore, natural
42
values of TSS ranging up to about 40 mg/1 and turbidity ranging up to about
26 NTU apJ;ear to be more realistic.
Effects ,gf Placer Mining ,gn Natural water Oualicy
The Below Sluice ranges and means presented in Table 9 were compiled from
data collected at all of the surveyed mine sites. Comparison of the below
sluice water quality to natural conditions demonstrates placer mining has a
detrimental effect on water qualityo Below sluice dissolved oxygen
concentrations and pH levels decrease to 95% and 96% of the above sluice
levels, whereas temperature increases by 14%. Settleable solids, TSS, and
turbidity increase to many hundred times natural conditions.
Data from those mine sites having a IX>nd or ponds during at least one of the
site visits were used to compile the means and ranges of the various
parameters for the Pond Influent and Pond Effluent categories presented in
Table 9. Water quality between the Below Sluice and Pond Influent sample
locations changed. Dissolved oxygen and pH continued to decline from natural
conditions and temperature continued to increase. However, these changes
were slight. Settleable solids, TSS, and turbidity levels~ although
significantly higher than natural conditions, demonstrated decreases between
the sluice and pond(s). Water quality also changed between the Pond Influent
and Effluent locations. The major chan,ge was the decrease in settleable
solids, TSS, and turbidity levels. Nevertheless, these levels were still
significantly higher than the natural condition levels for these parameter~
Dissolved oxygen continued to decrease slightly and temperature increased
slightly.
43
TABLE 9
RAN3~ AND MEANS OF MEASU:RED PARAMETERS 1\BO'IE, WI'llliN, AND BE.I.al PLACER MI~'ES
Total
Dissolved D.O., Settleable Suspended
Oxygen, Percent Temperature IiJ, Solids, Solids '1\lrbidity,
IDeation DQ/~ Saturatiw ~ a! Units ml/1 IIQI'1 Bm
14.0 111 11 7.7 0.1 67 55 Maxirnllll
Above 11.8 97 7 7.1 0.1 17 15 Mean
Sluice 9.8 86 3 6.0 0.1 1.1 1.0 Minimlln,
1.0 7 2.0 0.5 o.o 15 16 Stan.Dev.
13.0 106 12 8.2 240 69400 18800 Maximum
Be1CM 11.2 95 8 6.8 42 17500 7700 Mean
Sluice 8.2 73 5 5.6 4.0 1160 1800 Mininn.Jn
1.1 8 2 0.6 54 19700 4200 Stan.Dev.
12.5 105 12 7.5 160 33200 13400 Maximllll
Pond 10 .. 6 92 9 6.7 28 14700 6700 Mean
Influent 8.5 77 5 5.7 2.0 2230 1200 Minimum
1.1 8 2 0.6 37 9870 3500 Stan.Dev.
11.9 100 12 1.8 32 25700 8200 Maximum
lOOd 10.3 90 10 6.9 5.0 3940 3000 Mean
Effluent 7.9 75 5 5.6 0.1 410 160 Minimum
1.1 7 2 0.6 9~0 6660 2600 Stan.Dev.
12.2 98 12 7.6 4.0 6020 6400 Maximum soo• 10.7 92 9 6.9 1.1 1400 1700 Mean
Downstream 9.5 80 4 6.0 0 .. 1 2.2 7 .. 8 Minimum
0.8 5 2 0.6 1.4 1630 1400 Stan.Dev.
12.2 100 12 8.3 40 28000 10800 Maximum
Tailrace 10.7 91 8 7.1 10.3 7310 4000 Mean
8.3 75 5 6.3 1.5 500 1600 Minimum
0.9 6 2 0.6 10.7 7480 2900 Stan.Dev.
Data for two downstream locations are presented in Table 9, 500 • Downstream
and Tailrace. Data for the 500 1 Downstream sample location were compiled
from the sarne mine sites used to compile the means and ranges of the various
parameters at the pond influent and effluent locations. Data for the Tail-
race location were oompiled from the ranaining mine sites and these data were
measured at the farthest downstrecun sample site which was either the end of
tailrace or 500' oownstream from the tailrace. Data from the 500' Downstream
and Tailrace sample locations represent the quality of water that is returned
to the environment below placer mines. Also, these two locations can be used
to compare the water quality leaving mining operations having ponds as
opposed to those without !X)nds
Relative to the "tailrace" samples, water quality at the 500 1 Downstream
location displays a decrease in settJ eable solids, TSS, and turbidity, but
the levels of these parameters still remain markedly higher than natural
conditio~ Water quality at the Tailrace location, as judged by settleable
solids, TSS, and turbidity, was much worse than at the 500' Downstream
station. The Tailrace sample location levels of these parameters were
comparable to levels found between the pond influent and pond effluent
iocations •
.Effects .Qf P1acer Mining ,gn Arsenic Levels
Water samples for the laboratocy analyses of total and dissolved arsenic were
collected once, above and below, each of 15 mine sites. One mine site at
Livengood was intended to be one of the mine sites studied. HoNever,
operational problems at this site required that it be eliminated from the
44
study. The arsenic values are presented because they add to the relatively
small data base. Note that there is no data for Mine Site 15 on Porcupir1e
creek.
Dissolved and susp:nded arsenic concentrations measured at the 15 mine sites
are presented in Table 10. Furthermore, this table presents the range, mean,
number of observations, and standard deviation for these data divided into
four groups:
+ dissolved arsenic above t:iluice,
+ suspended arsenic above sluice,
+ dissolve:d arsenic below sluice, a1.1d 7
+ suspended arsenic below sluice.
'!be information in Table 10 indicates that the dispersion or variability of
arsenic concentrations, both dissolved and suspended, is quite high. Also,
arsenic appaars in higher concentrations in the susp:mded fraction than in
the dissolved fraction, and the below sluice levels of both fractions of
arsenic are generally higher than their res~ctive fractions above slui~.
'Tile data in Table 10 were s~jivided into a number of conditions that are a
better representation of arsenic corx:entrations at placer mines (Table 11).
First, data were separated into Natural Conditions and Disturbed Conditions.
This was necessary because a number of mine sites were operating on streams
where other operations were upstream or where there were other factors that
had changed the water quality from the natural condition at the arove slui~
sample location. It is worthy to note that the above sluice natural
condition is the only condition where dissolved arsenic concentrations
45
TA'SLE 10
Mine Site Sugnded Arsenic.mg/1
1 Above Sluice 0.0040 0.0026
250 • Below Pond 5 0.0033 0.0469
2 Above Sluice 0.0509 0.0027
At Washed Out Pond 0.127 11.0
3 Tom Creek 0.0038 0.0046
Gilmore Creek 0.0028 0.0061
Pond Effluent 0.0031 0.113
4 Above Sluice 01.0031 0.328
End of Tailrace 0.0002 0.425
5 Above Sluice 0.0002 1.54
End of Tailrace 0 .. 0063 0.823
6 Above Sluice 0,.0165 0.0109
Pond Effluent 0 .. 0060 0.339
7 Above Sluice 0.0041 0.338
End of Tailrace 0.0062 3.49
8 Above Sluice 0.0030 0.0004
500 w D<:Mlstream 0.0110 9.12
9 Above Sluice 0.0044 0.0365
Pond Effluent 0.0319 .1.12
10 Above Sluice 0.0026 0.556
500 • Downstream 0.0053 1.86
11 Above Sluice 0.0050 0.0225
500' Downstream 0.0060 0,.366
12 Above Sluice 0.0131 0.215
End of Tailrace 0.0089 0.541
13 Above Sluice 0.0002 0.0014
Pond Effluent 0.0002 0 .. 0016
14 Above Sluice 0.0083 0.0217
Pond Effluent 0.0017 0.990
15 Above Sluice 0.0002 o.o
In Pond Near Effluent 0.0002 0.0462
TABLE 10 (continued)
!hove Sluice Below Sluice
DiSsolved SUspended Dissolved Suapended
Maximum 0.0509 1~4 0.127 11.0
Mean 0.0076 0.193 0.0145 2.02
Minim \.It\ 0.0002 o.o 0.0002 0.0016
No. Ci:>servations 16 16 15 15
Standard Deviation 0.0124 0.396 0.0321 3.40
~~te: (1) Values presented as less than 0.0002 were calculated as 0.0002 mg/1.
(2) Dissolved and total arsenic concentrations were determined.
Suspended arsenic is the difference between those values. Suspended
arsenic at mine site 15 is 0.0 because both the total and dissolved
fractions were 0.0002.
TABLE 11 (continued)
SQSPOOED ARSENIC. rw/~
Natural Qmditians -Belcar Sluice -CUt-of-stream -With pgndQ
MaXimllt\
Mean
Minimt.Jn
standard Deviation
~. Cbservati.ons
0.0060 0.339
0.0032 0.1440
0.0002 0.0462
0.0029 0.1688
3 3
Note: Values presented as less than 0.0002 were calculated as 0.0002 mg,/1.
The mine sites from which data were compiled for the various conditions
appear below.
Natural Cooditions: 1,2,3,6,8,13,14 and 15~
Disturbed Conditions: 4,5,7 ,9,10,11 and 12.
With Pcll'lds: 1,3 ,6 ,13 ,14 ard 15.
Without Ponds: 2 and 8.
Instream with Ponds: 3 and 14.
OUt-of-Stream with Ponds: 1,6 and 13.
TABLE 11
ARSENIC <DNDITI~ E'OR VARlCUS LOCATIONS AT PlACER MINE SITES
Maximum
Mean
Minimum
Standard 0.:1~viation
No. CbseiVations
Maximum
~an
Minimum
Standard Deviation
No. CbseiVations
Maximum
Mean
Minimum
Standard Deviation
No. Cbservations
Maximum
Mean
Minimum
Standard Deviation
No. Cl:>servations
Maxi.1'[lum
Mean
Minimum
Standard Deviation
No. (]:)servations
Maximum
Mean
Minimum
Standard Deviation
No. CbseiVations
Natural ~ -Above .S.l.u.~
o.oso9 · o~o2.17
0.0100 0.0063
0.0002 o.o
0.0161 0~0070
8 8
Natural Conditions -.Be~ .Sluice
0.127 11.0
0.0191 2.71
0.0002 Oo0016
0.0438 4.58
8 8
Disturbed Conditions --~ Sluice
0.0131 1.54
0.0046 0.434
0.0002 0.0225
0.0040 0.522
7 7
.Disturbed Conditions -Below Sluice
0.0319 3.49
0.0093 1.23
0.0002 0.366
0.0103 1.12
7 7
Natural Conditions --Below Sluice -With Ponds
0~0060 0.990
0.0024 0.256
0.0002 0.0016
0.0022 0.379
6 6
Natural Conditio®--Below Sluice -H.ithout Ponds
0.127 11.0
0.0690 10.06
0.0110 9.12
0.0820 1.33
2 2
Natural Conditions --Below Sluice -Instream -With Ponds
Maximum
Mean
Minimum
Standard Deviation
No. Cbservations
0.0031 0.990
0.0024 0.552
0.0017 0.113
0.0010 0.620
2 2
typically exceed the sus}?ended arsenic concentrations. Also, the above
sluice natural condition suspended arsenic concentrations were significant~y
lower than the suspended arset1ic levels for the other conditions. Second,
the below sluice natural condition (data compiled from those mine sites
exhibiting undisturbed conditions above the mine but where arsenic samples
were collected downstream from the sluice) was divided into four groups: with
ponds, without ponds, instream with ponds, and out-of-stream with ponds.
Consequently, there are eight groups, 2 with disturbed conditions above the
sluice and 6 with natural conditions above the sluice.
The means and standard deviations of dissolved and suspended arsenic for the
various coooitions are noteworthy, and are presented below in Table 12.
The means and standard deviations of dissolved arsenic for four oondi tions,
including both disturbed conditions, are less than the above sluice natural
condition. Also, the standard deviation is less than the mean in each of the
first three conditions, one of which is disturbed. The mean and standard
deviation of suspended arsenic is lowest for the above sluice condition, but
the downstream from sluice natural condition had a higher mean and standard
deviation that all the conditions except the downstream from sluice without
ponds condition.
Effects .Qf _Surfa~ Loading .of Settling Ponds .on sedilrentation
An examination of the efficiencies of the settling ~1nds at the surveyed mine
sites in ranoving total sus~;ended solids indicates that only Mine Numbers 3,
6 and 13 achieved 90 fercent removal, or more, of suspended solids, see Table
46
TABLE 12
DISSOLVED AND SUSPENDED ARSENIC NEAN ~EN.I:RATIONS
AND STANDARD DEVIATION FOR VARIOUS OONDITIONS AT PLACER MINES
Downstream from sluice, instream, with ponds
Downs.tream fran sluice, with ponds
])a.mstream, out-of-stream, with ponds
Above Sluice, disturbed
~rnstream from sluice, disturbed
Above Sluice, natural
Downstream from sluice, natural
Downstream from sluice, without ponds
Above Sluice, natural
Downstream from sluice, out-of-stream, with ponds
Downstream fran sluice, with ponds
Above Sluice, disturbed
Downstream fran sluice, in stream, with ponds
Downstream fran sluice, disturbed
IkMnstream from sluice, natural
Downstream from sluice, without ponds
DISSOLVED ARSENIC, mg/ 1
Standard
Mean Deviation
0.0024
0.0024
0.0032
0.0046
0.0093
0.0100
0.0191
0.0690
0.0010
0.0022
0.0029
0.0040
0.0103
0.0161
0.0439
0.0820
SUSPENDED ARSENIC,rng/1
Standard
Mean Deviation
0.0063
0.1140
0.256
0.434
0"522
1.23
2.71
10.06
0 .. 0070
0.1688
0.379
0 .. 522
0.620
1.12
4 .. 58
1.33
!3. The range of surface loading of the p:>oos at these mines,as presented in
Table s, was between 760 and 1600 gpm per acre. Five mines had settling
p:mds that -~chieved removal efficiencies of total su9t=ended solids wit.llin a
range of 12 to 78 percent. The ponds at these mines had surface loadings of
between ·so and 23,500 gpm per acre. The demonstration settling pond at
POrcupine Creek achieved a removal efficienc:J of total suspended solids, of
only 60 percent,. the lowest of any of the ponds that were surveyed, and had a
surface loading of 2840 gpn per acre.
Despite a general parallel between total suspended solids and turbidity
values as measured in individual water samples, Drawing No. 5, no significant
relationship was detected between the efficiency of the settling porrls at the
surveyed mine sites in removing turbidity and the surface loading of these
ponds. The computed least squares linear relationships of the pond
efficien~cies, in terms of percent removal of turbidity, total suspended
solids and settleable solids to the :pond surface loadings had correlation
coefficients of 0.17 r 0.15 and 0.7 respectively. This suggests that other
factors affecting turbidity removal may be more significant then surface
loading, such as the Shape or grain size of the suspended particles.
Effects .Qf Particle Sizea ,gn sedinl;ntation
Gradation curves of paydirt sampled at the 16 mine sites are presented in
Drawings 9 through 11. Only one sample was obtained from Mine sites 15 and
16 on Porcupine Creek. The data is presented in tabular form on Table 13.
Notice only three mines have paydirt with more than 10% by weight of
particles having a grain size smaller than 0.02 mm.
47
•
Mi1ne
Site
TABLE 13
SEDIMENrATIOO EFlF'ECI'IVENF..SS AT S\ORVEYED PLACER MINES
% Removal
of Solids.
Predicted
·% Frcw
less than Settling
% 0.002 mm Columns
Recyc:le (';Clay compound) (T.S.S.}
Actual %
Ranoval of Solids
Setteabl~
TSS Solids
Surface
Loading
gpm/acre
Daily Discharge
of Soils
While Sluicing
Setteable
TSS Solids
{tons) (cu. yds.}
Canpliance
With Standards
.2ml/l
Setteable 25NTU
Solids Turbidity
Mines. With. Sett.llng Ponds
1·* I() 2.7 66.7 72 86 14500 15.1 6.5 NYN N
2* 0-:SO 0.1 98.5 78 100 750 12.7 18.3 Ylti N
3 :90 1.5 71.1 91 99 1200 2.6 0.4 y N
6 0 0.4 84.4 90 99 1600 9.6 0.8 y N
B** 0 1.9 84.6 74 98 3850 46.8 49.7 N N
91 80 1.4 84.2 73 81 23500 4.8 31.4 N N
13 0 0.4 99.6 98 100 760 1.6 0.4 y YN
14 80 3.0 97.0 76 85 3460 0.3 0.1 YNN N
16 0 &/A 87.4 60 97 2840 7.3 3.1 56Y33N N
Mines Without Settling Ponds
4
5
7
10
11
12
15
*
**
Notes:
0 0.6 60 38 77 68 N N
0 0.6 -24 38 192 272 N N
0 (~ .3 65 33 85 222 N N
0 ().9 33 0 100 357 N N
0 0.4 71 69 196 298 N N
0 0.8 30 13 80 87 N N
0 WA 41 82 20 122
Trip 1 only
Trip 3 only
1) % Removal of solids measured across p:>nd, where present. Where no settling p:>nd was present the indicated %
removal is determined for tailrace.
2) "Y" indicates the standard was met and "N" indicates the standard was not met. One Y or one N means the
standard was met every time the parameter was measured. For Mine Sites 1-14 three characters are used to
indicate whether the stand was met during all or only one or two site visits (Mine Site 13 was only visited \
twice). At Porcupin·e Creek, settleable solids met the standards part of the time during the 50-day sample }··
period. :rhe numbers of times the standards were and were not met are presented for those ..P3ramete.cs. j
~~~~~~~~~~~~~~~~~~~~~~~~. ··~u••J:~~~·~~•~~~~~~~•r. -~-~ ~ pa~·-~•IMt•~;•~ ~-·~c¥n~ut~~-lQM~t·J·tJIIU~Jf~
A strong relationship was found between the amount of small sized particles
in the material being mined and the effectiveness of settling ponds in
reducing the levels of turbidity and total suspended solids in the sluice box
discharge.
This relationship is illustrated in Drawing 13 in which the percentage
removal of turbidity and suspended solids in the settling ponds is plotted
with respect to the percentage, by weight, of particles smaller than 0.02 mm
in the material being mined. Similar relationships were found when the
percentage of other particle sizes, between 0.002 mm and that passing a No.
200 sieve, was used in the compariso~
The strength of the relationship between the relative amount of fine grained
particles in the material being mined and the ob.served efficiencies of the
settling pond suggests that, as might be expected, the efficiency of a
settling pond is more sensitive to the particle size distribution of the
material being mined than to the size of the p:>nd, the flow rate throu,Jh the-·
pond, or any of the other variables that have been considered in this study.
By sedimentation theory, suspended solids in a settling basin that have a
downward settling velocity that is equal to or greater than the surface
.loadng of the basin (i.e., the ratio of the flow rate through the basin to
the basin surface area) will be retained in the basin as sediment. Suspended
particles having a lesser settling velocity will remain in suspension in the
basn discharge,
The settling velocities of the smallest particles retained in the ponds of
48
TABLE 14
SETrLitti POW DEK>NSTRATIOO PIDJECI'
PARI'ICLE SIZE ANALYSIS OF f.'IA'l'ERI1\L Fla-t PAYDIRT
u.s. Standard Sieve Q;2enings, .Ina. u.s.~, Standard Sieve Nunbers Grain Size, nm
Mining
Site ~lL2. ~ U! .l.L2 UB. ~ 1.0_ 2.0. .4D. .5.0. 100 2D.O. 0.02 0.005 0.002
1 89.1 P.t: ,. ~;;J.4 83.6 80.5 78.8 73.9 64.7 54.3 44.3 42 .. 6 37.0 13.0 12.2 4.5 2.7
2 93.5 87.4 80.5 69.1 62 .. 9 49.6 39.5 29.9 22.8 19.4 14.2 10.1 1.3 0.3 0.1
3 93.7 87.4 83.6 78 .. 5 75.1 67.4 60.9 54.1 48.1 43.4 33.6 27.5 7.7 2.4 1.5
4 95.1 88.4 83.2 77.4 73.1 65.8 59.2 53.6 47.0 42 .. 1 32 .. 2 23.0 5.7 1.8 0.6
5 98.5 94.1 89.0 79.6 74.4 60.1 45.8 35.7 24.4 17.5 9.4 5.7 2.6 1.2 o.,6
6 93.3 93.3 88.8 81.7 77.6 67.7 56.3 42.9 31.5 26.5 21.0 16.4 3.5 0.8 0.4
7 96.0 96.0 89.8 77.7 70 .. 1 52.8 40 .. 5 29 .. 2 20.1 15.6 10.0 6.4 1.2 0.4 0.3
8 95.5 91.4 87.3 82.9 79.5 74.8 71.6 69.2 63.8 60.5 55.8 52 .. 1 14.8 4.3 1.9
9 100 95.5 91.9 90.2 89.5 87.8 86.6 85.2 83 .. 2 79.4 60 .. 0 34.9 5.9 2.0 1.4
10 92.8 84.7 79.4 69.8 < 62.5 49.1 39.7 31.8 26.5 24.2 21.1 18.6 3.8 1.5 0.9
1"" .~ 84.0 69.8 61.6 51.5 46.8 35.6 25.9 17 .o 10.9 8.6 8.1 5.3 2.9 0.9 0.4
12 99.0 87.1 81.2 73.0 69.0 60.5 53.4 46.0 39.6 35.8 28.6 22.0 5 .. 5 1.9 0.8
13 92.1 83 .. 3 78.7 70.7 63.8 48.2 37.2 28.5 22.6 19.8 15.7 12.4 2.6 0.9 0.4
14 97.1 93.4 88.8 84.6 81.5 75.1 69.3 63.3 58.0 54.7 47.6 41.1 14.0 5.1 3.0
16 90.0 80.0 57.0 39.0 25.0 14.0 8.0 6.0 4.0 2.2
lbte: Data indicated for sieve analyses are percent passing, by weight. Data indicated by grain size are the
percentage smaller than the indicated size, by weight.
r DraWUlc..J 9
....... t~ J::t • 1J ••• •. • t.
I
l::
~ 40 ,_
Q)
a..
l I • • i I : " I l i ! j ! '\. 3 ~ r:-~~ . I! r-H·. -~ ---ft·--1 r Tt~--r-·-: \ '
p..:.-1--i -· . . ........... ~ . ~ t-+---P~.._H~-+-+-tl--+---t--+-----l
• • I ! ' t I I' L: I . ' I i ; I . I ' 20 ri-r-r ~ . . --· --. ' -·;·· -. ---.......... I -r...-·-r-·t--· . I I -+----r-f--t-:l'k-r'\-t-1~--!1---+----1
! I i ; ' l ! U· . : ! : . "io..l : : : I I I • : I I Hi ~-:-: · --··-· --,! 1--r .... -"7 ·-··r -~------· ! r... -r-r---r-·-j--···--r;,.---r+-+-t---t-·· ~ ',
IQ ma:. I • j_ ___ .. -... -+J-tl ,--7-+-+--7-·· . ._.:. ---++-,l 1'-~~·::,:--r-· , I -r---
• • I I l: 1 l I . i ... I-... I, I ['....
o 1 ~----=:UJ.~l~~-1~----~~~~-~~m+l~~-~~~~-~~~ --
40
50
60
70
eo
90
100
100 5J 10 5 I 0.5 C I 005 0.01 0.005 0001
Gratn S1ze tn Millimeters
I -GRAVIT'"--=r_=------SAND I SILT or CLAY
CoQill_--=-.r. Ft n e .. ~~L~Q.o"'O;~·-r-._··:_~-M'.!!-.::::.:e-a~::u:m~~~,...I~....-_-_-_-_-....:.--F....:.i~n-e=-------~~-L-----·--------·--=-_]
SAMPLE NO. MOISTURE DRY
CON1 ENT OENSJ'";"'T ?t LL CLASSIFICATION a DESCRIPTION
...
QJ en ...
0
0
l.) -c:
Cl)
(.)
\..
<U a..
~-------r-----r-----T--------------------+------------------------------------------------------·----~
1----------1------t-----t-----t-· ---·-1----t------------------------------------------·---1
I------1-----+---T---·---.------·-~----+-------------------------------------------------------~
~--------~-----+------~-----4------4-----~~-----------------------------------------------------------------------~
~---··------~·-----+------;------------------+--·-----------------------------------------··-· -
1-------1-------+-------r------r-------f-·---r--------··-··--·-·-----------·-·-··--·----------------
I
Ft $ ~L----~C~O~N~S_U __ L_T_A_N_T __ S_~_•_N_C_. __ __
PORCUPINE CREEK SITE
SETTUNG POND DEMONSTRATION PROJECT
DRAWN BY LOS . ··--·-----11
APPROVED BY WA t--·----·-------1 ~'-ti --11/24/81
PROJECT NO. 013104
Drawing 10
IJ S Standard Sieve Openmgs m Inch liS U.S. Stondcud Sutvt Numbers
3 2 11/l I l/4 112 3/8 3 4 6 8 10 14 16 20 30 40 506070 100 140 200 270 roo I i". I I' I 'I I I I I I I' I ! I I I'
90 I ! I !
80 'l
70 -.s=
Cll c; :r: 60 I
>.
.Q
'-.,
!::: 50
u.. -c • 40 u ...
CD a..
30
• I ; . ~
! I I
20
I l . I !
10
Gram S1z ~ in Millimeters
SILT or CLAY
SAMPLE NO CLASSIF,CATI.JN a DESCR1PTtON
---t---·--·. ----· ----·---·-----·-·
_______________ , __ ·-.. ----··-· ···-
----+----------· --· -· -·--·--··--
0
10
20
30
40
50
60
70
I
I' .,
+---· 80
i
90
roo
0001
....
.s::. 1:. .,
:r:
>.
..0 ...
CLI rn ....
0
0
(.) -c
CD u ...
q)
a.
-------
1----·--4-----t----·-t-------· ~ .. ----·-----" ----... -.. -·-~ ·--· ... -·-
ft $ ~----c_o __ N_s __ u_L_T_A __ N_T_s_. __ rN __ c_. __ _
--··--. ·-.. ---... --------------1
GRAIN SIZE CURVES
SETTLING POND DEMONSciRATION PROJECT
:::::--
-----------------------------------------------,, . . '
Ut...Wlnq 11
"l".i-·J~ .~.·~
I sc
70 -I .c ::n
Q;
~ 60
>..
.0 ...
Q) : 50
lL -c .,
40 u ....
Q)
Cl.
30
20
10
.. f ":t • II' • >f. ••
·:
f' ...
l
2.0
30
I 40
I
60
70
90
IOC
0001
c.
fl', ....
c c
'' -c
(!;)
u ...
<V
Cl.
--GRAVEL ' I SAND
_ __,__--.::Co:::::.arse l Ftne ·-•..• _ Course.__._ __ "'""M;...;:;;e..;;;;..a·;..:;:u;...;.;;m.;...____._l ___ ....;F:....:i~n.:..e ___ __.. _______ s_u_.::r_o_r_r_,L_A_Y _______ __,
,.., SAMPLE NO MOtST•JRE DRY
\..OI'<TENT DEI\J'liTY -L
11-------i'-----t---·----
R $ M....._ __ c_o_N_s_uLTANTS, INC.
CLASSIFICATiuN a DESCRIPTION
~···---·
-------------------· --·-·---·--·-·---·------------
·------· -·--·------------·-------------·---·
-------·----·. ··-·--------·--·-·-·---------t
-·-------------------------------------,-----------~~--~ DRAWN BY LOS SIZE CURVES
SETTLING POND DEMONSTRATION PROJECT
APPROVED BY .WA
DAT~------11/24/81
PROJECT NO. 013104
'!
100
9C
80
70 -.s::.
t:l'
iii
~ 60
>.
.0
.....
ell c:: 50
IL ... c
4D 40 0 ...
4P a..
30
20
10
Drqwing 12
U S Standard S•eve OptninQI .n lnchn v S Standard S1e11e N;Jm"!l•r• litdromehr
3 2 I 1/l I ~ 1/2 3/6 3 4 6 8 10 14 16 20 30 40 506070 IOU i40 200 2.70 0
I i I
II .
I j .
I
I I l \_ ·~~
i-+-t-1--t-+--
\ '·" '!o.. :._' I'
r-\, /Site r·~
I
I
I
10
20
-30 .s::.
01
Q)
~
40 >.
.0 ...
tU .,
50 ...
0
0
CJ ... c
i I -,~ ! '·r-. ~'--..... I I\ so. .,
0 ....
Q)
:•PY
oc.:~5·T t
0..
70
I
--' r
_j 80 l
I
90
--100
0001
J
Gratn S1ze m Millimeters_ _ __
~M::..:..;e:...:o:..:..:u=~=A-~~ L Finc ___ -_~-]_ ____ .. _____ _:~LT_ o_r_c_LA_Y ___________ _,
C~...ASSlFiCAT ,;,. a JESCRIPTION
--------------~------------------·---------1
•• _ .... --· ·--·,---.. --· __ ..... ,.. •• <>~ ----·--.. ···-·""'·'"-
--..... -.... ... ___ .. _"" .. ·-.. -~ --.. -.. --....... -... _.. ---··~ .. --,.··-.. ~----,., __ ... ..._ __ ...,. ~--· ... --....... -
R ¢ M.___ __ c_o_N_s_u_L_T_A_N_T_s_,_, N_c __ _
GRAIN SIZE CURVES
SETTLING POND
~-,
I'
I
r
I
t
' .
LA
. '
•
15
10
1-5
X
(,!) w
~
>-Ill
Total Suspended Solids
• aM CDNIIUL.TANTII,INC.
2 •
E 0 '------'----,.,....j'-----~----'----_. e o 20 40 so eo 100
C\1
0
d
z
4
:t:l5
1-
a:
UJ
..J
..J
<t
~ en
~10
0
0
Turbidity
0 20
Numbers indicate assigned
mine site numbers.
9
0
40 80
'Yo REDUCTION
!00
EFFECT OF PARTICLE SIZE
ON SETTLING POND EFF1CI.ENCY
SETTLING POND DEMONSTRATION PROJECT
l
--==~------------------------------------~--------------------__;
rve"ed mine sites can therefore be determined by dimensional conversion the su... '.l
of the surface loading of each pond, to velocity units (a surface loading
lOOO gallons per minute per acre of pond surface is equal to a settling
l l·ty of 0.184 feet t:er hour, or 0.0156 mm/sec). ve oc
r.lbe size of the smallest p3.rticle :-etained by sedimentation in the p:>oos is
that size at which the proportion by weight of particles larger than this
size in the su~ded solids entering the r:ooo is equal to the efficiency of
the pond in removing total suspended solids. In this report, the pond
removal efficiency is defined as the ratio of the difference in concentration
-of total suspended solids entering and leaving the pond to the concentration
gf total sustended solids in the pond influent.
Thus, if the pond. removal efficiency and the distribution of particle sizes
in a fX'nd influent are known, the size of the smallest tarticle retained by
sedimentation in the pond can be determined. In this study, the
determination of the particle size distribution of sus:p=nded solids in the
mab~rial ent~ring the settling ponds was rr;t directly included as part of the
collected daca. This size distribution was approximated, hc·wever 1 by the
assumption that the sust:ended material entering the settling J;X>nd '1lould be
represented by ~~e distribution of the particle sizes included in that
traction of the material being mined that passed a No. 50 sieve. The
particle s:ize distribution of the -No. 50 fraction of the mat"c';r~.l'l being
mined is presented in Table 15 each mine site. When these distr1uutions are
plotted on semi logarithmic scale, similar to Drawings 9 through 12, the size
Qf the Srn(tllest particle retained by the pond can be _determined by
interpolation, according to the rationale described above. The particle
49
TABLE 15
Distribution of Particle Sizes of Fraction Passing No. 50 Sieve
(Percentage STna.ller Than Indicated Size, By Weight)
Grain Size, nm
Mine lQ.,. .300 .150 .075 ..Jl2. .illl5 .002
1 100 87 31 29 11 6
2 .. 73 52 7 2 l
3 n 77 63 18 6 3
4 II 76 55 14 4 1
5 It 54 33 15 7 3
6 n 79 62 13 3 2
7 n 64 41 8 3 2
8 n 92 86 24 7 3
9 n 76 44 7 3 2
10" II 87 77 16 6 4
11 II 94 62 34 10 5
12 " 80 61 15 5 2
13 If 79 63 13 5 2
14 n 87 75 26 9 5
15/16 " 96 77 43 13 6
Note: Particle size distributions are for Nos 50 fractions of material from
paydirt.
l
sizes thus determined for each of the mines having settling ponds are
tabulated in Table 16. Also tabulated is the surface loading of each pond.
This is defined as the ratio of the flow through the pond, in gallons per
minute, to the surface area of the {X>nd, in acres. It is noted that the pond
surface, loading, its overflow velocity, and the settling velocity of the
smallest particle retained by the p:>nd are equivalent parameters, expressed
in different units. For refermce, each are shown on Table 16.
•'
The theoretical velocity of small spheres in a fluid, according to Stokea
Law, is as follc1ws:
V = g(P-Pi)d2
-RM
where v = relative velocity batween the particle and the fluid
g = gr~avitational acceleration
M = kinematic viscosity
P a\!ld J?i = specific gravities of particle and fluid respectively
d = particle diameter
K = a constant
When the particle sizes and overflow rates presented in Table 15 are
subjected to a. least squares fit, a semi-empirical relationship between the
particle size.s and settling velocities determined in this study can be
defined by m~)ifying the above equation to the form where a and b are
regression coefficient~
v = a + g(P=Pil g2.
bM
Data from Mines 1 and 2 were not included in the least squares analysis since
the indicated re:lationships between particle size and settling velocity at
these two mines differed stbstantially from those of the other mines. This
50
Percent of Total
Suspended Solids
Ranoved by Pond
Mine Site (See Table 12)
1* 72
2* 78
3 91
6 90
8 74
9* 73
13 98
14 76
15/16 60
TABLE 16
SEDIMENTATICE CHARACTERI8.riCS OF ~
~QUi AT SURVEYID PLN.'ER Mll£8
Percent of Total Diameter of
Suspended Solids Smallest Particle
Remaining in Retained by
Effluent ~"'iJ, mm
28 0.018
22 0,032
9 0.007
10 0.012
26 0.021
Z7 0.042
2 0.002
24 0.016
40 ().018
;
Surface Loading POnd
(Overflow Rate)
(See Table)
mm/sec ft/hr
.226 2.67
.012 0.14
.019 0.22
.025 0.30
.060 0.71
.367 4.34
.012 0 .. 18
.054 0.64
.. 044 0.52
* Data not used in lea,st squares regression of particle size and surface loading values
gpm/acre
14,500
760
1,200
1,600
3,900
24,000
760
3,500
2,800
r
l
J
difference may have been the result of differences in the distribution of
particle sizes in the material samples from the mine cuts at these mines,
compared with the normal distribution of particle sizes in material placed in
the sluices boxes at these sites. Although data from Mine 9 were in general
agreement with the other data, this data were also excluded from the least
squares computation because the extremely small settling pond at this site
(0.08 acres) resulted in a settling velocity that averaged alx>ut an order of
magnitude greater than the other mines. As such, it was felt that this one
da.ta set would unduly affect the least squares fit of the rest of the data.,
The semi empirical relationsip between settling velicity and particle
diameter, as determined by the least squares fit of the data from the six
mines having ponds (exclusive of Mines 1, 2 and 9 for the reasons described
above) is as follows:
Vs = 0.013 + g(P.-Pil d2.
115 'M
Where the paraneters are expressed in the following tmits:
Vs -Millimeters per second
g -Millil'reters per second per second
d -Millilreters
M -Centipoises
This semi empitical relationship, together with that of Stokes Law, is
presented on Drawing 14.
Using this semi empirical relationsip and the distribution of particle sizes
presented in Table 15 the percent of total suspended solids that would be
expected to be removed by a settling pooo was computed for different settling
S.l
I
I
I
I
I
'
. '
..
, J
. ·~
•aM CaNeULTANTe.INC.
Semi Empiricgl Btlationshio
Vs = 0.013 + g (P-Pj) d2
115M
100,000
Stokes Lgw
~ Vs=g(P-Pj)d2___ ~
~ 18M 10.000 g
e,o-' ~--------~~--------~~--~----~ ~ E
Colloidal Ra e LIJ
1-
1,000 ~
100
~ ~ a:: w > 0
to-3 t-------r---+-----lf---------1..
Specific Gravity= 2.70 10
1o·4 -... ............. ...-.............. .____.__.__,_......,.......,......_.....~.__. ....... ~......,.
JQ-4 to-3 to-2
PARTICLE DIAMETER, d, in mm
Vs = settling velocity, m m/sec
g =gravitational acceleration, mm/sec2
P = specific gravity of particle
P; = specific gravity of the fluid
M =kinematic viscosity of the fluid
d = particle diameter, mm
.timJ. r Data points are numbered
according to mine I ocotion.
DAT•
12-7-8.1 •c:•&..•
AS SHOWN
PARTICLE SETTLING VELOCITIES
SETTLING POND DEMONSTRATION PROJECT
CH.CK•a •v ... a..a.C:T ND• DIIAWINCI Na •
WA 013104 14
' . I
I ' I • I.
I ,
' ..
I
I
I
I
I
I
I i
IJ
I
I
I
I
I
I
I
I
I ' l •
i l ..
velocities. This is plotted on Drawings 15 through 22, together with the
data ,points for field measurements in this study, and removal efficiencies
that were predicted from settling column test results. From these
relationsips, one could predict the efficienqy of sediment removal at each
mine site if the size of the surface area of the ponds or flow rates were
changed.
Hater !hie
Drawings 23 through 27 schematically present the results of flow measuranents
within E?ach mine site. Minor losses and infl()WS are not shown. Significant
inflows that could be estimated but nO't measured are shown. A few sites show
an increase in flow in the downstream direction, this is attributed to
groundwater. inflow.
For comparison, water use· and settling pond characteristics are presented u1
Table 8. The average water use dut'ing sluicing at mines having settling
p:mds was 2,600 gallons p:r minute (1.17 million gallons per day of 7.4 oours
working)while mines without ponds used an average of 3,600 gallons per minute
or 1.62 rng/day with the same average workday. This difference can be
attributed to the use of material classification equipment at many of the
mines that have settling ponds. The removal of the coarser material front the
paydirt with such equipment allows the remaning material in the paydirt to be
processed throught the sluice box. using a lower water flow.
Table 7 lists the range in gallons required to sluice one cubic yard for each
mine site. Mine sites #7, t9 and 113 had the lowest water use: 300, 560 and
52
I
l
J
l
I
I.
I
I
1
fl ,$,
lj
r
L 00
:;u:1
r:: 1:1
7'-3
6 [1
5 (1
40
3 ~3
t l.:) -~
'1LZ1
::0
~':' ~~
.; t:1
50
•t (1
.3 (1
i I
·.-.! I
~~1
a1j
'B a~ CI)OJ
!:::3U
en~
~~
tU
MINE 1
Relationship fron1 Settling Column T~sts
Semi empirical relationship from field measurements
~ ~-r---r---+-·-+-~+--+----i---+
0 1 2 ? 4
Settling Velocity, Ft/Hr
a a:~·•····•····'····'··i·• o ·s,ooo 1o,ooo 1s,ooo 2o,ooo 2s,ooo
.. .. I C/)
~ t ..... ..... ~
~ ~: r· rg !
'B T ~~, , ~r tr.l ~
3 a!l
~ -r ~-
J
!-
0
Surface Loading, gpmVacre
r:u~ 2,
Relationship from Settling Column Teets
_,..,._, ______ ------r
................. __ ----+
Semi empirical relationship from field measurements
Field Data
t--·t---+----t-·--+--··-t-. ·-~
1 2 3 ·~
Settling Velocity, Ft/Hr
f q I ~ d 0 I I I l ~ f e ~ b I r , ~ I ~~ • ~ ~ 0,0 1616 0 l,000,02rOOO
SUrface t;,ading, 9pt\lacre
RELATIONSHIPS~ SET11JIN3 VEI.DCI'l.Y AID REMJVAL OF 'lOTAL SUSPEWEO SOLIDS
SETTLIN; FOND DEK>N8l'RATION PinJECr
: . : I aCA&..•
. :
·I
~-----------------------------------------~
l J
I I
I l
I I
I 1
~ ~I
l I
0
MINE 3
"'ield Data ;'Relationship from Settling Column Tests
----,.,. ... ------... ~
·~~--~ ..... .., __ "+
Semi empirical relationship from field measurements
+----·+--+--+----1---+
1 2 3 4
Settling VelOCity, Ft/Hr
I I I • • t I I , t , I I I ' ' I ' I
5,000 10,000 15,000 20,000
Surface Loading, gpm{acre
MINE 4
25,000
Relationship from Settling Column Tests
__ _.. __ ....., ___ --+
~------... +
Semi empirical relationship from field measurements
+----<+----+---+ ----+·---t ---+
1 .. : :. 4
Settling Velocity, Ft/Hr
I I I I I I • I I I I I l I I I I l I I I I J
0 5,000 10,000 15,000 20,000 25,000
surface Loading, gpm(acre
RELATIONSHIPS BE'IWEEN SE'ITLIOO VEIOCITY AND REK>VAL OF 'IDTAL SUSPENDED OOLIDS
SErrTLING OON:> DEK>NSI'RATION PPaJECr
0
~
11
, ___ a_A_T_·---'---·-C_A_L_·.__.l__a_A_A_W_N_•_v_.J_C_H_•_c_K_•_a __ ._v__J_ .. _A_a.J __ ·.,C--T-N_a_ . ...,L_a_A_A.='f~6~1 N_Q_N_a_.
~;
[
<
<
I'
(
t (1 (1
9 (1
·:: •3
7 l:1
6 ~3
5 ~3
40
3 (1
40
MINE 5
I ...
t1l Relationship from Settling Column Tests '0 ·~ 1 ....-tr-4 ~~ ~Jt a~+ ~ § t ~~
fl gi-
'Semi empirical relationship from field measurements
~-~--+--+--+--~--~--1
0 1 ~ 3 4
Settling Velocity, Ft/Hr
l1 J•ltltal liiLIII!tlt!lli
0 5,000 10,000 15,000 20,000 25,000
I
Surface Loading, gpm(acre
MINE§
Relationship from Settling Column Tests
...... -... -.... --.. ----_, ..
~~ -----
~~ empirical relationship from field measurements
Field Ot3.ta
~----+---+--· t-
1
+t --4f ---+---;--·-~ -. -=~
Settling Velocity, Ft/Hr
I I I I J I I I I I I I I I I I I I I I ' I I l J
0 5,000 10,000 15,000 20,000 25,000
surface Loading, 9IltV acre
REf.ATIONSHIPS BETWEEN SETI'LIOO VELOCITY AND REIDVAL OF TOrAL SUSPENDED SOLIDS
SE'.rl'LI:OO rom DEM:>NSTRATION PIDJECT
CIAT. 8CA&.• DIIIAWN DV
------------------------------------------------------------------~, -
-
1-~
!
j
li
[l
~ l I
'
~
[
[
(,
~
"aM CON •uLTANT.,INC.
MINE 7
1 t1 0 .... ~ I
Relationship from Settling Column Tests
til I ~ t
r-lr-4!
~~~
rg)i 'B I <J>+l: 0.. c ..:.
tll<ll'
::JUJ
Ul lo.l I
------------+
------~
Semi a~pirical relationship from field measurements
.-t~T .s l ~o r ~ I
30 .; --1--·-t-__,-+---l----~1----t---·-+--f.
(t 1 2 3 4
0
Settling Velocity, Ft/Hr
I I I ! I I I I I I I I I I I I I I I I I I
5,000 10,000 15,000 20,000 25,000
Surface Leading, gpn/acre
MINE 8
1 o (1 r
~ f Relationship from
Settling Column Tests til ' '0 1
·r-f
l"""ir-1;
~ ~ +
'0 ~ l w~· ~) rg !
------------------+
Semi empirical ~elationship from
field measurements :;.) ~@ f(
:; ::. ~ & -r Field Data
~o ~ r ....... ........ -..... I ~+
--1---1--+-·--+---+--+---t---+
I) 1 2 3 ·~
Settling Velocity, Ft/Hr
I -1 I I I I I I I I I I t ' I I I I I I I I I I I
0 5,000 10,000 15,000 20,000 25,000
Surface Loading, gpm{acre
RELATIONSHIPS BE'IWEEN SETTLIOO VEIDCITY AND REMJVAL OF 'roTAL SUSPEIDED SOLIDS
Sm'rLIOO row DEMJNSI'RATION PRlJECT
l l'--__ a_A_T_·_-"'--l __ ._c_A_L_. _ __.~l.__D_R_A_W_N_._v_"'--C-H_•_c_K_•_a __ •_v__.._P_R_a.J_•_c_T_N_a_ • ..._a_iii_A_W,;;;,lS,;..I_N_ca_N_O-J.)
~-··--·
~
IJ ,_
fJ
~l
t
' l
IJ ' ' '
~ '
j
IJ'
' !
~ ' I
~ '
'
101.) ...
::n::1 ~ ~
r-tr-tj
::: ~ J t
.;.o ~~I
:::) C) r ens..+
so 3~ I
Ill S. M CON 8ULTANT.,I NC.
MINE 9
Relationship from Settling CoJ L~H·r~ 'f<~st~~
_-"'11111_......, ____ ..., -1-
~ield Data
empirical relationship frou. fic-·ld measurements
40 e3 t
l---~---+---+--I ~-+--i--+
30
I I
0
I I
0
1 2 1 4
Settling Velocity, Ft/Hr
's!obo' ilb}o~ '1~,boo' 2o,doo I 2s',cloo
Surface Loading, gprn(acre
MINE 10
Relationship from Settling Colunn Te.sts
--......... -.. --.
..... _ ---+
Semi Empirical relationship from field w~asurements
I I I I I t \ I I • I I l f I ' I I I ' I t '
5,000 10,000 15,000 20,000 25,000
RELATIONSHIPS BE:lWEEN SE"I•J.'LIN:; VEI.DCI'lY AND REMJV.AL OF 'lOTAL SUSPENDED SOLIDS
EE:rl'LlR3 R'JND DEKJNSTRATION PROJECt'
L.__-__ a_A_T_· __ _._ __ ·_~. A~~--' ] . D Aa:'_N_a_Y-.a-..C_H_•_c_M_._a __ lli_Y__.._ ...... A_G_._~ •_c_T_N __ O_ • ......_O_R_A_f_g_•_N_Q_N_a. l
-----------------------------·-----------------------------------------------------'-------~-------------------·~----------------------------------------
.l
~ :
l
•; f.)
IJ '
'
.
[
!
'
'...)
II
j
•.
)
[1
~
~"
I
L
R&M CQN8ULTANT.1 fNC.
MINE 11
Semi empirical relationship from field measurements
------+ -----.............
Relationship front Settling Column Tests
~--~~~-4---+---~~~--~
0
I I
0
t ~_1 o ... r
~ L
·.-t I
r-ir-ij
·:: (1 ~~r
ro ~ !
?:j ~ ~ !
c :
.:; (1
1 ~ 3 4
Settling Velocity, Ft/Hr
5,000 10,000 15,000 20,000 25,000
surface Loading, gpm(acre
MINE 12
Relationship from Settling Column Tests
--..... --..........
----~ ... -..... -+ a -:5 L
Ul ~ I 05 ..., 1-
r-i~: ItS I
Semi empirical relationship from field measurements
~ ~·) .u l _o i
~ I .
f-. --r---+--+---·+---+---+----·-f---+
0 1 ..::: ;. ··t
Settling Velocity, Ft/Hr
I I I I I I I I I I I I I I I I I I I I I I I
0 5,000 10,000 15,000 20,000 25,000
Surface Loading, gpm{acre
RElATIONSHIPS BE'IWEEN SETI'LIN:; VEI.OCI'n ANa REr-DVJ\L OF 'lOTAL SUSPENDED &:>LIDS
SET.ILIOO rom DEIDNSTRATION PmJEC'l'
•cA &.• OIIIAWINQ NQ.
20 -------'------~'-------.....a-------'--···-,__ ____ ,...__..:.;::;...._ __ _.
~----------~----------------------~~
j I
I]
I!
,,
')
11
;
' J
1?,,· .t r ~
[ '
'
0
AAM CONSULTANT.,INC.
tUNE 13
Relationship from Settling Column Tests
--... _ ---+
Semi empirical relationship from field measurements
..__-+-1 +---+--~--+----i---+
1 ~ 4
SettlintJ vcl.ocity, Ft/Hr
I I I I I I I I I I I I I I 1 I I I I I I l
5,000 10,000 15,000 20,000 25,000
Surface Loading, gpm(acre
MINE 14
. ~Relationship from Settling Column Tests
.. T~~. ~ nl ~ Semi empi;~;:el:ti~n~hi~ • from field measurements
~ :> l
r:-i i ...... ' QJ I ;-' .-1 "0 ...
a~l
Ul ~ I bS 1-1 I
'5(1 ~t
4D r· +
I
Field Da.ta
'"' ~ ------....
+---1---+·--·+---+--+--· -+---t--···-\-
l) t 2 ? •l
Settling Velocity, Ft/Hr
l I . L I I I I I I I I I I I I I I I I I I I I f I
0 5,000 10,000 15,000 20,000 25,000
Surface Loading, gpm(acre
R.EIATIONSHIPS BETWEEN SET.l."'LIOO VElOCITY AND REIDVAL OF 'rol'AL SUSPENDED SOLIDS
Smw!LI:OO roND DEIDNSTRATION PRQJECr
(
'----~---------.--1)·.
l
1~--------------------~
" & M CQN 8UL.TANT8.1NC.
I~
l
; ,
(' '
I
·'
F1
' ;
(: ;
I
l )
' \
)
~
MINE 15/16
Relationship from Settling Cblumn Tests
Semi empirical relationship from field measurements
--------+ . t---+---+--' +-__ ..,.__-1---4------{
(I 1 2 3 4
Settling Velocity, Ft/Hr
l I'' 1,.,,1, ,,,,,,,,(,,,,I
0 5;000 10,000 15,000 20,000 25,000
surface wading, 9PlV' acre
~ (..__ __ a,_A_T_• __ ~_· _•_c_A_L._._---c~.&..~-a----~~~-A_w_N_-_•_v--JI.._c_H_•_~_IC_--._G_· __ •_v......~.l_•_"_a..a_. a_c_T_N_a_ • ..~.l_a_ ... _ .. -'2;=~~·-N_a.,_J]
L-----------~---------------~----------------~---------------J
~~--------------------------~
I ~·
'
_:
t;;
_;
1 ..
E~)
J:.'
IL
~;~
~.
lJ"
l: ~~
l
~~
Mine Site I. Fl SH CR£EK
TRIP THREE ONLY.
NO MAP FOR TRIPS ONE AND TWO
PfJIId EHiuMt
• 4.$ Cf$
, r $(){)~,
4./cfs • . t
Mine Stt. 3. GlLMORE CREEK
AVERAGE FLOW OF THREE TRIPS
NOTE: Minor Jo•• and minor inflowa not shown
... ,. .. .....
If -9-81 NONE
... M CONIIULTANT.,CNC.
j
AboiM Sl;ic. •
0.? cfs a
Pt:Jnd lnflu•nt
/. J'Cf$
500' lJownsttWim I
1.8 cfs l
~ Billow S/UiCII 11.5 cfs
Mine Site 2. FAIABANKS CREEK
AVERAGE FLDW OF THREE TRIPS
\
Mine Site 4. EAGLE CREEK
TRIP THREE ONLY.
NO MAP FOR TRIPS ONE AND TWO
Pl..ACER MINE WATER USAGE
SETTLING POND DEMONSTRATION PROJECT
a
WA 2'3
h ~~ ..___ _______________________ ..., ·~:
lu
f.,
·'I
1-.
'' ; '
..... :--"
~·,
' ;
-~· ... :
t.,
'
'
_ ..... t
~~
~ £ag/tl CrHk
\ A/JtNI Pump
• N.S. _....\\
\----\a Below Sluit~
\ /'2cls
\ A-.... L~s to
/)" Tailings
-,/ ""
\,~"' E'nri of Ta!lraetl
~ II cis
500' Oownstream l
78 cis ,
Mine Site 5. EAGLE CREEK
TRIP TWO ONLY. NO MAP FOR TRIP ONE
" Faith CrHk / ·l A/Jove Pump
(
'-N.S.
B.YIXi» /"\.
9.0cls i / \
r-J Fl \! ~Below \ OYiriC/fl(/ IDW \ • Sluice
J 9.3 cis
/ \ Faii/J
Pond lnllutlnt ./ ) CrHk
19cfs
)
w: .. -r
: Pond Efflut1nt
I
I
I I t II cis
[~.·~ :, Mine Site 6. FAITH CREEK
J! TRIP ONE ONLY.
i~ NOTE: Minor losses and minor inflows not shown.
l I 1·9·81
•aAL.8
NONE
.. aM C:DN.ULTANT8,1NC.
Eag!B C,_k \
Abov' $~ 1---~ &low SluiM
~ 7.8 cfs ~ ,\ ( \ \')
\ . /End of Tal/roc.
(• 13 c.fs
I 500 DownstrtJOm \
N.S. '
Mine Site 5. EAGLE CREEK
TRIP THREE ONLY.
\ Faith Cr!Mk By Pump
• 160 cfs (EJ
/~
lhlow Sluice ~ )
?.i'cfs •
!%,• \ J/ t
Pond lnflutlflf i \ II cfs t Foltll
Crtl•k
Pond Effluent
5.7cls
I
)
j
Mine Site 6. FAITH CREEK
TRIP TWO ONL~ NO MV' FOR TRIP THREE
PLACER MINE WATER USAGE
SETTLING POND DEMONSTRATION PAOJECT
CHIIOIC8D
WA
••wttweN&
24
I
!
I
I II I
I
1]
L~· ------~~~================~
,,
I~_:
[;
(:j
1,:
'' _,
,_
r·
f!.:i
l
L~
M,lne Site 7. MAs·roooN CREEK
TRIPS TVJO AND THREE ONLY.
NO MAP FOR TRIP ONE.
16 cfs • '=-}
500' Oownstr•om -Mine Sit~ 7'
28c~ f
Mine Site 9. MASTODON CREEK
AVERAGE FLOW OF THREE TRIPS
~, I NOTE: Minor Iones and minor inflows not shown.
IICIAt.•
NONE
I l I I ~ \V > Prmtf Effii!Mf \ • I 4.7 cfs
~~
5001 t:Jt:Jwnslream \
5.1 cfs \
Mi n\l Site 8. MILLER CREEK
TRIP THREE ONLY.
NO MAPS FOR TRIPS ONE AND TWO
\
\ Above Pump R:¥1d rr;;./ \ 3/ cfs
&bwSiuic.J-e:s, I
6.7'cfs } 29cfs)
\ f Mammoth
~:: \ 1 Crt~Bit
7.7cfs
400' Oowns7r;;, \y
on Bypass 38cfs ·
Mine Site 10. MAMMOTH CREEK
TR! P ONE ONLY.
PLACER MINE WATER USAGE
SETTLING POND DEMONSTRATION PROJECT
CMIICICIID •v lltt~~ew•crr NO. a.AWINe Na.
WA 013104 25
I
I
I
i
-----------~---------------------------
f, ~~
~~
!.
~J
~
~-----------------------------~------------
\ A/1ov. Slui~
• 23 en
Mine Site 10. MAMMOTH CREEK
TRIPS TWO AND THREE
O«KKwood CrMJk
l'!cfs
Btl/ow SluicfJ
10 cfs
l 500' Oownstnam
• 26 cfs
\
Mine Site 12. DEADWOOD CREEK
TRIP TWO
NO MAP FOR TRIP ONE
NOTE: Minor losses and minor inflows not sMwn.
• aM C:GNIIULTANTII,INC.
{u--~
tooo'~srua) f
\ Abow Sluic.
29cfs
13cfs ~ (
\ . ;;rooMd CrHk v---24cfs
/ 500' Oownstr«rm I .J8cfs
Mine Site II. CROOKED CREEK
TRIPS TWO AND THREE
NO MAP FOR TRIP ONE
8.4 cfs
Dt10rlwootl CrHk f
s.sm~
II cfs
500' Oownslr.am \
19cfs '
Mine Site 12. DEADWOOD CREEK
TRIP THREE
PLACER MINE WATER USAGE
SETTLING POND DEMONSTRATION PROJECT
11-9·81 NONE WA 013104 26 -------L-_:.:=.:.:.::..__L__.=:__..L_....:.:::.__....L_~:.:.:::..___Jl-_.,,, ____ _,
-----
I I
I
. ------------------------------------------------~~~ :~~----------------------.~&MC~~~~.IN~C-.---~ ~ \ ilyJKu$ Abov~ Sluice J "'•~4 cfs ,..,;
~ \ / ~ B.tow Sluics
f: ., _.
[.,
'
.~ ... }
· -....... 3.2 cfs
~
r ~ ... Pond £fflufJnf
3.3 cfs
Mine Site 13. CHENA RIVER
ALL TRIPS
'-Flume~: Crs.k .......... a 4 crs ....,.,-,
/ \\ ' c )
Abo.,. Slulc• / J j
Q2cls ,/'' · ·· -•,.../Pond Influent
~ a?c~
f \ Pond Effluent
~ 1.1 cfs
f ' / l "--'--""
500' Down!ifftl(lm \f);
Q9cfs "
\
Mine Site 14. FLUME CREEK
ALL TRIPS
NOTE: Minor 1~1 and minor inflows not shown. PLACER M! N E. WATER USAGE
SETTLING POND DEMONSTRATION PROJECT
DAT•
II-9-81
•eA&.•
NONE
..
j
1
1
l
gallonS per cubic yard sluiced, respectively. Mine site 47 u~~ an
39{)..:.520
nt of "Atley Bowl" centrifugal classifiers to reduce water use. a.r.rangeme
tl3 used a vibrating screen a.nd trammel to presort ~ydi.rt prior:-to Mine site
A vibrating screen was used b.y ~ine site #9 to redur;~ water use. sluicing ..
'f rm flow in natural and artificial chann~ls is commonly repre.sent~d by Unl o
Manlling' 5 equation in the form:
_ l s~o D.33 8 0 .. 5 Q -., l'U';,
n
in which Q is the volume of flow per ~Jnit time
A is the cross sectional area of flow
R is the hydraulic radius, deferred as the area A divided by the
wetted permeter
s is the slope that the channel bot tan makes with the horizontal v and
n is .Manning's coeffieient, an empirlcal coefficient having the
dimensions of L 1/6 that remans relatively constant for a given
boundary condition, regardless of depth of flow or channel size or
slope.
Measurements of sluice box slopes and dimensions and depths of flow were
included in this study, as well as the flow through the sluice boxes. Thus,
the empirical rouglmess coefficient "n" in Manning's equation can be computed
for flows thro~Jgh sluice boxes. Table 17 presents the results of sluice box
measurements. Since flow measurement could not be taken in side channels of
sluice boxes the flow was assumed to be divided equally in each channel~
Also flow measurements used in these calculation were measured 2-40 feet
downstream of the sluice box.
53
Mine
Site
tb.
1
2
3
4
5
6
7
8
9
10
11
12
13
14
Creek
Fish
Fairbanks
Gilmore
Eagle
Eagle
Faith
Mastodon
Miller
Mastodon
~1arrmoth
Crooked
Deadwood
Chena Piver
Flume
Porcupine
Sluice i2
(old box)
(new box)
Water 1 Depth
In coos
4
2
1,3,1
1,4,1
4,4,4
~,1~,~
3,8
3,3,3,3,3
4,6,4
3~
3,3,3
6
2,5,2
TABLE 17
MANNIN;'S n VALUE FOR SELECTED SLUICE BOXES
Sluice box =l Inches
36
18
24,33,24
26,26,26
18,33,18
72,48,72
48cf62
24,31,34,31,24
48,48,48
24
10,17,10
36
18,36118
Nl.IIlber of
Channels
in Sluice-
box
1
1
3
3
3
3
2
5
3
1
3
1
3
Flowr
cfs
Q
1.2
6.8
6.8
7.8
8.8
8.2
8.0
4.3
12
12
0.25
1.00
1.08
1.92
1.00
4.44
3.00
4.67
0.58
0.77
1.50
1.75
Hydraulic
Radius,
ft.
R
.137
.136
.. 144
.248
.061
.404
.207
.327
.225
.168
.375
.233
Slope,
Pet
s
0.1584
0.1405
0.1405
0.1584
0.2679
0.1584
0 .. 1405
0.2309
0.0612
0.1250
0.1250
0.1250
Manning's
Roughness
Coefficient
n
.033
.022
.024
.058
.014
.072
.010
.029
.034
.029
N:>te 1: Multiple listing of water depth and width are the depth and width in the side channel, center channel and side
channel of the sluice box. Sites with dashes indicate value was not measured. Sluice box measurements were
taken at the flows listed.
The equation for computing Manning's rouglmess coefficient is: n = 1.4.9. A R 2/3 s 1/2
Q
' '
I '
--
" "value was determined to be 0.032, with a standard deviation of
The mean n
The relatively large variation in "n" values is prc,bably the result o.o19· .
h ighlY tur:bulant flow through the sluice boxes. Manning's equation
of the ·
e s uniform flow, which sluice boxes do not have, due to riffles and as sum
rocks in the channels ..
4.6 ~IONS
The following conclusions are drawn from the data collected from the mine
sites that were sutveyed in this study:
1 .. The effluent from placer mine sites typically does ·not meet all State
and Federal water quality standards. The standards for turbidity and
arsenic were almost never met and the standard for settleable solids
was only met about half the time. The pH and temperature standards
were met most of the time, and the standard for dissolved oxygen was
met all the time.
2. Only one of the mining operations studied met essentially all State
and Federal water quality standards, as measured 500' downstream from
the point of discharge into the receiving stream. This site was
located off-stream, had less than 3% of material smaller than 0.02mm
in the parent material, utilized material classification, a long
tailrace, multiple ponds with baffles in the final pond, and had or
approx~ately thr~fold a of dilution in the receiving stream.
3. Wi~h respect to water quality, it was shown that mining operations
having settling ponds released higher quality water than operations
without ponds. However, even with ponds, settleable solids values
were usually 10 times higher, and turbidity and total suspended
54
solids levels were· usually about one hundred times higher than
natural oondi tions-:
4. Arsenic concentrations appear in higher concentrations in the
suspended fraction 'than in the dissolved fraction below the sluice
and downstream from the sluice. Concentrati0ns of both fractions
below and downstream f+om the sluice are higher than their respective
fractions above the sluice.
5. Mines that do not use screens or other material classification
apparatus to remove oversize material prior to sluicing typically
require about 50 percent more water than mines having classification
S¥Stems. This higher water usa results in a requirement for larger
sedimentation p:>oos to achieve a given quality of effluent discharge.
Also, a correspondingly larger volume of flow in the receiving stream
is required to achieve a gl~;en level of dilution of the discharge.
The effectiveness of a sluice in gold recovery is generally improved
by pre-sluice classificatio~
6. Manning's equation can be used to provide a general approximation of
flows through a sluice box. Field measurements of sluice box flows
indicate a mean roughness coeffici,ent of n = 0.,032 with a standard
7. Consumptive use of water by placer miners is slight. The majority of
water diverted for use is returned for use by miners downstreameither
directly through overland flow r or indirectly through groundwater
infiltration
Be Turbidity values, in NTU, have been found to be typically about 140
percent of total suspended solid concentrations, in mg/1, up to a
concentration of about 3500 mg/1. Above this value, turbidity levels
55
increase by about 200 NTtJ for each 1000 mg/1 increase in the
concentration of total suspended solids.
9 • The relative frac::tion of clay and. silt sized particles in the
material being mined is the most critical parameter affecting the
efficiency of sedimentation in settling ponds. A good correlation
between sedimentation efficiency and the amount of fine grained soil
in the paydirt can be obtained without consideration of pond size,
discharge flows and other variables.
56
SEcriON FI'\,;r.:
SUMMARY
State receiving water btandards and the standards presented in placer mining
permits have been com~'red to levels of the various parameters measured
downstream from each mine site that was surveyed in this study. Of these
above standards, dissolved oxygen was the only parameter that was within the
standard at all mine sites and at all times that dissolved oxygen was
n-easured. The pH sm"ldard was met at 12 of 15 mine sites and met part of the
time at the other three sites. Settleable solids also exhibited variability
where some sites met the standard (3 of 15~, others did not (8), and some met
the stand~rd part of the time (4). Seven of the nine mines having settling
ponds met the standard at least part of the time~ No mines without settling
ponds rnet the standard. Turbidity and arsenic standards were not met at 14
of the 15 sites.
Only one mine site (13) can be considered as having met all of the above
standards. Although turbidity at Mine Site 13 exceeded the standard during
the second site visit, the diffE!rence between the standard (natural condition
~?f 8.4 N1U plus the allowed increase of 25 NID, or 33.4 Nr.U) and the measured
turbidit·· level (34 NTU) is too small to be significant.. The site had the
least water use, the greatest degree of classification of the material being
mined by particle size, ptior to sluicing, one of the lowest clay contents of
the material being sluiced, and a high receiving stream dilution factor.
57
' ,,
' ,'
. '
h the turbidity that would result from a given concentration of AlthOU9 .
nd ed solids is quite variable at low concentrations and would be
suspe
Cted to be substantially affected by particle size, color, and other expe
variables, the relationship between the concentration of total suspended
solids and turbidity that was developed in this study indicates that the
following concentrations of total suspended solids would result in the
approximate turbidity levels as indicated below:
Total Suspended
SOlids I fil/1
2.5
7
19
Turbidity, Nm
25
50
100
Thus, very high sedimentation efficiencies are required in order to meet
turbidity standards or permit conditions.
The data obtained in this .study indicate that the amount of small soil
particles in the material being mined (in the silt, clay and colloid size
ranges} is the most import~nt single factor affecting settling pond
sedimentation rates. From these data it has been determined that suspended
particles of the sizes given below would be de};X)si ted as sediment in settling
ponds having overflow rates that are equal to or less than t~ following:
?article Size, nm
.00.2 .oos
.010
.020
(1050
.010
58
~ Bate· gpn/acre
860
1,000
1,500
3,700
19,000
65,000
This would suggest that, for maximum sedim~~tation efficiency, placer mine
settling ponds should have a surface area and discharge rate that would
resUlt in overflow rates of not more than 860 gpm per acre$
59
SECI'ION Sl.X
REF~
Alaska Department of Environmental Conservation (1979). Placer Mining and
Water Quality. Jtmeau, Alaska, Noverri:>er, 100 W•
Alaska Department of Environmental Conservation (1979). Water Quality Stan-
dards. Juneau, Alaska, 34 pp.
Alaska Water Laboratory (1969). Effects of placer mining on water quality in
Alaska.. Federal Water Pollution Control Administration, College, Alaska,
91 pp.
American Public Health Association, et al. (1971). Standard methods for the
examination of water and wastewater, 13th Edition. American Public
Health Association, New York, 874 w.
Clark, J.W.; w. Viessman Jr; and M.J. Hammer (1971). Water Supply and
Pollution Control. International Textbook Company, New York, 661 pp.
calspan Corporation {1976). Final Report: Water quality data at selected
placer mines in Alaska .. calspan CorpJration. Buffalo, New York, 49 H?•
Calspan Corporation (1979). Evaluation of wastewater treatment» practices
employed at Alaskan gold placer mining operations. Contract. No. 6 8-01-
4845, u.s. Environmental Protection Agency, Effluent Guidelines
Division. Washington, D.C., July, 44 pp. * Cordova, A.J. and Kelley, DW (1960). The influences of inorganic sediment
on the Aquatic Life of Shearrs. California Fish & Game, 1960,
H? 189-229.
Department of Indian and Northern Affairs (1981). Water use technology fo~
placer mining effluent control. QS-Y006-000-EE-Al .. Whitehorse, Yukon
Territory, 71 pp.
Madison, R.J. {1981). Effects of placer mining on hydrologic systems in
Alaska. u.s Department of the Interior. Bureau of Land Management.
Technical Report No. 7. Anchorage, Alaska, August, 32 W·
Mineral Industry Research Laboratory {1979). Effect of placer mining on the
environment. Contract No. J0177134, u.s. Department of the Interior,
Bureau of Mines~ Washington, D.C., June, 33 R?·
u.s. Environmental Protection Agency {1976}. Erosion and sediment control -
surface mining in the eastern u.s., 2 volumes. EPA 625/3-76-006,
Washington, D.C., October, 102 w. and 136 pp.
u.s. Environmental Protection Agency (1976). Quality criteria for water. u.s.
Environmental Protection Agency, Washington, D.C., 255 R?·
Webber Jr., W.J. (1972). Physiochemical processes for water quality control.
John Wiley and Sons. New York, 640 J;P.
Zemailsky, G.M.; T.Tilsworth; and D.J. Cook (1976). Alaska mining and water
quality. University of Alaska. Institute of Water Resources. Report IWR--
74 113 W·
60
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S~IR; OOLUMN DATA
MINIOO SITE 1
0 HOUR 6 HOUR 12 HOUR
Depth, TSS, Turb, TSS, Turb, TSS, Turb,
Feet rrq/1 NIU ng/1 Nru rrg/1 NIU
1.5 Port 6 3680 3000 930 4300 1240 1600
3.5 5 6060 2700 1270 2700 1640 2000
5.5 4 5980 3800 1530 2000 1850 2300
7.5 3 9390 3800 3120 2400 2000 1900
9.5 1 6310 2800 4720 2900 3570 3400
24 HCUR 48 HCUR 72 HOOR
Depth, TSS, Turb, TSS, Turb, TSS, Turb,
Feet ng/l NlU rrg/1 NlU ng/1 NIU
1.5 Port 6 730 1300 680 1100 450 1000
3.5 5 910 1800 1560 1600 800 1500
5 .. 5 4 1380 1900 1600 1700 730 1400
7.5 3 1440 2200 1060 1500 1020 2000
9.5 1 1840 2200 1280 1600 890 1400
Corrrnents:
r t ; ...
L ..
L.
SETI'LOO OOLUMN DATA
MINII-13 SI'l'E 2
0 HOOR 6 HOUR 12 HOUR
Depth, TSS,. Turb, TSS, 'l.urb, TSS, Turb,
Feet mg/1 NlU Irg/1 NlU rrg/1 NIU
1 .. 5 Port 6 43800 10600 7490 6200 3000 4500
3.5 5 40000 15600 9920 6700 4130 5800
5.5 4 64500 17300 9920 7900 4100 5000
7.5 3 66800 13100 33700 7400 5300 6100
·9.5 1 72900 17200 382000 23000 442000 7400
24 HOOR 48 HOOR 72 HOOR
Depth, TSS, Turb, T'"'...,S, Turb, TSS, Turb,
Feet ttg,/1 mu ng/1 NIU rrg/1 NIU
1 .. 5 Port 6 1380 2500 660 1500 450 1000
3.5 5 1780 2900 840 1800 490 1200
5.5 4 1910 3100 890 1700 910 1200
7.5 3 2110 3200 800 1700 630 1300
9.5 1 455000 23000 424000 23200 263000 24000
Comments: The total suspended soils and turbidity values for the 9 .. 5 foot
depth are considered to be a non representative sample. Sediment accumulating
in the bottom of the column was drawn off with the sample. Compaction occurring.
between 24 and 72 hours is the likely reason that the 48-hour and 72-hour TSS
and Turb levels decreased.
1
1
1 .
" t
I .
SETrLOO CDLDm DATA
MININJ SITE 3
0 HOUR 6 OOUR 12 HOUR
Depth, TSS, '1\lrb, TSS, Turb, TSS, Turb,
Feet mq/1 NIU rrg/1 NIU nq/1 Nru
1.5 Port 6 7440 5600 4660 5400 3600 6900
3.5 5 11700 7400 2300 6400 4210 5100
5 ~-·~., 4 9150 6700 3360 7200 3800 4800
7.5 3 14000 6200 3050 7700 4690 4800
9.5 1 13700 7500 3690 5900 4100 5000
24 HOOR 48 HOUR 72 HOOR
Depth, TSS, Turb, TSS, Turb, TSS, Turb,
Feet ng,/1 NlU ng/1 NlU ng/1 NIU
'" 1.5 Port 6 3140 4000 3260 4300 1960 3400
3.5 5 3300 5000 3910 5400 2610 3900
5.5 4 4240 6200 2910 4300 3140 3800
\.vi 7.5 "l 3430 4800 3290 4500 3160 3900 ~
9.5 1 3870 6100 3630 5000 3150 3600 ,,
;'
~ .. --,
Ccmrnents:
·)
SE':MLI~ OOLUMN DATA
MINI~ SITE 4
0 HOOR 6 IDUR 12 HCXJR
Depth, TSS, Turb, 1~S, TUrb, TSS, Turb,
Feet ng/1 NIU ~n;V'1 .N!'U lll:Vl NIU
1.5 Port 6 29100 11500 3260 6200 1780 4300
3 .. 5 5 28400 11300 4970 5900 3450 4000
5.5 4 34600 11800 4590 5900 2440 5100
7.5 3 37000 9600 6050 7500 2830 2700
8.5 2 7680 8300 2960 3900
9.5 1 38400 9300
24 Hcr.JR 48 fDJR 72 HOOR
Depth, TSS, Turb, TSS, Turb, TSS, Turb,
.Feet mg/1 mu mg/1 NllJ nq/1 ~Y]ll
1.5 Port 6 1000 1500 510 1300 170 1300
3.5 5 1430 3200 580 1700 150 1300
5.5 4 1180 2200 430 1300 110 1300
7.5 3 1720 2900 560 1500 190 1500
8.5 2" 1820 1800 640 1900 350 1600
9.5 1
Comrrents:
SETrLIOO <.DLUMN DATA
MINIR; SITE 5
OHOUR 6 HOUR 12 HOUR
oepth, TSS, Turb, TSS, Turb, TSS, Turb,
Feet rrg/1 mu ng/1 N1U mg/1 Nl'U
1.5 Port 6 3370 3000 2700 2700 2240 2200
3.5 5 4320 3400 2690 2500 3070 3400
5.5 4 6080 5900 4070 4300 3260 2600
7.5 3 7150 7400 5270 5300 4410 2500
8.5 1 6480 6700 5200 6400 3300 3200
24 HOOR 48 HOUR 72 HOUR
Depth, TSS, 'furb, TSS, Turb, TSS, Turb,
Feet ~l !:I""'U mg/1 NrU rr":l/1 Nlt1
1.5 Port 6 1240 2600 1050 2000 610 1400
3 .. 5 5 1760 2900 1190 2600 860 1400
5.5 4 1700 2600 1240 2700 980 1900
7.5 3 2370 3800 1460 1800 1050 1700
8.5 2 2110 2600 1440 2500 1530 2000
Cooments:
S&1!1'Lrm OOLUMN DATA
MINI!G SITE 6
0 HOOR 6 fiJUR 12 BJUR
Depth, TSS, Turb, TSS, '1\lrb, TSS, Turb,
Feet rng/1 N1U ng/1 NlU ng/1 NllJ
1.5 Port 6 4580 2400 1870 2100 1860 1400
3 .. 5 5 5060 3700 2990 2600 1830 1600
5~5 4 6080 2500 5630 2000 1610 1400
7.5 3 8590 3900 5010 2500 1680 1900
8.5 2 16200 3000 5760 2200 2290 1700
24 IDJR 48 IIXlR 72 HOUR
Depth, TSS, Turb, TSS, Turb, TSS, Turb,
Feet mg/1 N1U nq/1 Nru Il¥311 NIU
1.5 Port 6 880 1100 630 900 480 850
3.5 5 1220 1100 820 900 860 1400
·s.s 4 1330 1200 1140 800 1020 1300
7 .. 5 3 1470 1500 1170 1300 990 1400
8.5 2 2130 1400 1900 1600 710 1100
Catroents:
• "' 'I
Depth, r,
if Feet
1.5 Port 6
[;' 3.5 5
:t, 5.5 4 •' 7.5 3
9.5 1
~{
,l
[i i Comments:
i
I
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SE'l'lLOO <DLUMN MTA
MININ3 SITE 7
0 HOOR 6 HOUR 12 BOOR
TSS, Turb, TSS, Turb, TSS, Turb,
rrg/1 ng/1 NIU rrg,/1 NIU Nr'J
17200 6700 2710 3000 116J 2300
21800 6100 3040 2600 lP~O 2700
14300 5900 2260 2900 1670 1900
15800 5800 2950 3000 1890 1700
17100 6900 2850 2600 2090 2400
SE'tiLitG CXUJf9l DATA ..
MIHilG SITE a
0 HOOR 6 HOUR 12 HOUR
Depth, TSS, Turb, TSS, Turb, TSS, Turb,
Feet Dlg./1 HIU lg/1 NrU mg/1 mu
l .. S Port 6 11.100 ,,00 2550 34CO 1870 2000
3.5 5 -ll.SQO 7100 2830 2400 22.:SO 2500
5.5 4· 15400 5800 2930 2800 2380 1800
7.5 3 11600 4500 3010 3000 2450 2300
8.5 2 19100 5800 ll.60 3300 2510 2800
24 fiXJR 48 HCXJR 72 HOOR
Depth, TSS, Turb, TSS, Turb, TSS, Turb,
Feet 8111·. lliU 111]/1 NIU ng/1 N1U
1.:5 Port' 1390 2.00 970 1600 615 800
3 •. • !) 5 2020 1900 1420 2200 1100 750
5.5 4 200C 2100 1710 2100 1220 850
7.5 3 1640 20GD 2050 1800 1350 2000
8.5 2 2210 :2,00 1"180 1800 1380 1700
Carments:
MINIR; SITE 9
0 HOOR 6 BJUR 12 HOUR
oepthr TSS, Turb, TSS, Turb, TSS, Turb,
rrg/1 Nl'U ng/1 NlU rrg/l NIU peet
POrt 6 11300 7900 1610 2400 760 1500
1.5 5 12300 10600 2450 3900 9'\0 1600 ).5 4 9240 7200 2850 5300 1180 2600 s.s 3 14700 7400 3130 7000 1330 2100
7 .5. 2 16000 6200 3520 5300 1440" 2500 8.5
24 HOOR 48 HOOR 72 HOUR
oepth, TSS, Turb, TSS, Turb, TSS, Turb,
Feet ng,/1 N1U rrg/1 NIU mg/1 NIU
1.5 Port 6 670 1100 300 500 160 300
3.5 5 660 1200 300 400 180 500
5.5 4 730 1300 290 500 170 400
7.5 3 720 1700 380 850 100 550
8.5 2 730 1100 400 750 270 360
~nts:
SET'l'LIN:; COLUMN DATA
MINIM; SI'IE 10
0 BOOR 6 HCXJR 12 HOUR
Depth, TSS, Turb, TSS, Turb, TSS, Turb,
Feet nq,/1 NlU mg/1 NIU ng/1 m.u
1.5 Port 6 16700 7400 2930 5000 1730 4000
3.5 5 18000 7700 4810 4000 3620 5800
5.5 4 17900 6900 5020 5900 4190 4800
7.5 3 17000 7000 5600 6200 4460 4300
9.5 1 21000 8200 6400 6700 4850 6600
24 BOOR 48 HOUR 72 BOOR
Depth, TSS, Turb, TSS, Turb, TSS, :rurb,
Feet ng/1 mu m;v'1 NIU ng/1 l\"'IU
1.5 Port 6 1940 4000 1440 2200 1230 2300
3.5 5 3180 5000 2280 2800 1910 2600
5.5 4 3760 5300 2770 4200 2250 3200
7.5 3 4010 5300 2960 5600 3230 2900
9.5 1 4500 6100 2710 3000 2840 3800
Carments:
SE'l'ILIN:; CDLUMN DATA
MINIOO SITE 11
0 HOOR 6 HOUR 12 HOOR
Depth, TSS, Turb, TSS, 'Iurb, TSS1 Turb,
Feet mg/1 Nru ng/1 tm.J Iif3/1 Nl'U
1.5 Port 6 2400 2700 1530 2100 1270 1800
3~5 5 3040 3000 1610 2500 1480 1600
5.5 4 2890 2900 1860 2400 1410 1700
7.5 3 3250 3000 1750 2100 1600 1600
8.5 2 3560 1800 2125 3000 1590 1700
24 HOUR 48 HOUR 72 HOUR
Depth, TSS, Turb, TSS, Turb, TSS, Turb,
Feet I00_/1 NlU n~/1 NIU mg/1 .mu
1.5 Port 6 1100 1700 940 3000 750 1600
3.5 5 1130 1700 1040 2000 930 1600
5.5 4 1360 2000 1530 3800 1030 2400
7.5 3 1590 2100 1680 2600 1420 2400
8.5 2 1240 2600 1560 1500 1720 2100
Corrments:
SET!'LIN:; <DUJMN DATA
MDITR; SITE 12
0 HCXJR 6 HOUR 12 HOUR
Depth, 'l'SS, Turb, TSS, Turb, TSS, Turb,
Feet ng/1 NlU rrg/1 NIU rrg/1 mu
1.5 Port 6 19900 9600 5120 6400 3000 5400
3.5 5 25100 9400 5020 5900 3740 3900
5.5 4 13800 8600 8220 7500 4300 3800
7.5 3 21300 8900 6980 6600 4580 7000
8.5 2 7410 7500 5260 6400
9.5 1 23400 7900
24 HCXJR 48 HOUR 72 HOOR
Depth, TSS, '1\Irb, TSS, Turb, TSS, Turb,
Feet m;/1 NlU n-q/1 NIU rrg/1 NIU
1.5 Port 6 1170 4200 1420 2500 610 1600
3.5 5 2010 6600 2240 3000 1380 2200
5.5 4 2040 4800 1890 3900 1090 2600
7.5 3 2860 3600 1930 3700 1370 3000
8.5 2 2820 2300 1730 2600 1110 2800
9.5 1
Contnents:
SEITI'LI~ <DLDm DATA
MININ3 SITE 13
0 HOOR 6 HOUR 12 HOOR
Depth, TSS, Turb, TSS, Turb, TSS, Turb,
Feet mg/1 Nl'U rrg/1 Nru nq/1 NIU
1.5 Port 6 23900 9400 360 1000 290 750
3.5 5 27000 9600 770 1200 330 800
5.5 4 27000 8400 2000 1600 390 500
7.5 3 29000 12000 :<100 2000 410 500
8.5 2 3.2600 11500 22:t.: 3100 1020 850
24 HCXJR 48 HOOR 72 HOUR
Depth, TSS, Turb, TSS, . Turb, TSS, Turb,
Feet rng/1 NlU rrg/1 NlU rng,/1' NlU
1.5 Port 6 70.0 400 50.0 140 10.0 100
3.5 5 190 320 40.0 170 36.0 85
5.5 4 210 240 44.0 150 48.6 120
7 .. 5 3 300 320 76.0 280 44.0 160
8.5 2 220 360 51.5 140 76.0 80
Colrarents:
I
'· •
·'
MINI!~; SI'fE 14
0 HCXJR 6 HOOR 12 HOOR
Depth, TSS, 'l'urb, TSS, Turb, TSS, Turb,
Feet mg/1 !ftU ug/1 NIU rrg/1 mu
1.5 Port 6 21,00 10900 1840 1900 352 500 ' 3.5 5 26700 8300 2390 2500 380 450 .
J.
5.5 4 29400 10900 3310 7200 310 500 I
1 7.5 3 25000 12500 11900 10200 640 800 :j.
8.5 2 25700 13100 32500 12000 990 900 J
24 IDJR 48 HOUR 72 HOUR
Depth, TSS, Turb, TSS, Turb, 'I'SS, Turb,
Feet llg/1 N!U -.11 NnJ Jrg/1 mu
1.5 Port 6 180 450 68.0 100 12.0 60
3.5 5 100 400 64.0 120 20.0 40
5.5 4 250 360 84.0 130 24.0 45
7.5 3 320 320 68.0 110 52.0 45
a.5 2. 310 320 60.0 170 68.0 34
Catments:
APPENDIX II
sample Site Descriptions and Methods of Data Collection
1te foll~ing are descriptions of samples sites shown on Drawing No. 1.
~luice - A staff gauge was established 40' above the influent to
1. ~ater reservoir. When the miner working sluice f2 moved upstream ~e staff gauge was relocated approximately 150' above the water
2.
3.
4.
5.
6.
7.
B.
s.
eservoir. After a cat ran over the staff gauge, it was relocated a
r . rd and final time approximately 500' above the water reservoir. This ~e was sampled all fifty days. Water quality samples were taken in
the center of the channel near the staff gauge.
12a,il!l ~ss -This site was sampled on days when the water reservoir
overtlowed, a total of 22 visits. A staff gauge was installed 20'
downstream frcm the crest of the darn. The staff gauge was re-
established twice due to pond modification and heavy rains. The water
quality samp1es were taken in the center of the bypass near the staff
gauge.
ueger pqrcypL1e Creek -Water quality samples were taken approximately
500' above sluice tl. antis is the only "natural conditions" sample site
on Porcupine Creek. The site was sampled twice a week starting on Day
29 for a total of 7 visits.
aelQH Sluice -Water quality samples were taken approximately 10 seconds
after the loader dumped paydirt on the slickplcte and approximately 5'
to the left sida facing the sluicebox outfall.. Flows were recorded 40
to 100' downstream depending on a suitable channel. This site was
sampled for 20 visits.
Ianl<ee Creek -Water qUc'llity samples were taken approximately 20' above
the influent to Porcupine Creek. Flow measurements were taken at the
same loca.tion as the water quality samples. This site was sampled twice
a week starting on Day 23 for a total of 9 visits.
Settling fond .o.a.m Leak - A leak developed in the settling pond darn on
the right side looking downstream. WeLter quality samples were taken
from this leak starting on Day 16 for a total of 24 visits Flows for
this sample si.te were estinated.
Aboye Pond-A staff gauge was established and water quality samples
were tak-en 100• abo,le pond #1. This site wa.s discontinued after Day 15
due to high flows. A total of 10 sample visits were made .•
Below Bmd -A staff gauge was established and water quality samples
were taken 100' below the t:Ond. 'rhe pooo was built by the miner working
the trammel to settle out the suspended sediment added by the two miners
upstre~11. ~hls site was discontinued after 15 days due to high flows.
A total of 10 sample visits were made~
~.fond -· Water quality sample.:> were taken at the surface of the pond
next to the pump. No flow measurements were taken at the site. The
sampie site changed when the pump pond was moved upstream between Days
14 and 15. A total of 43 sample visits were made.
Sample sites 10-14 were sampled twice daily.
10. Below Trammel -Water quality samples were taken 20' below the end of
the sluicebox and awroximately 10 seconds after paydirt was added to
the hopper. Flow measurements were taken 300' downstream. A staff
gauge was·established but removed due to sediment deposition. The
sample site was relocated upstream when the trommel was moved upstream
between Days 14 and 15. '!he site was sampled for a total of 62 visits.
11. Pond In£luent -Water quality samples were taken 15' above the settling
pond. Flow measurements were made between 15 1 and 50 1 above the set-
tling pond depending on the best channel section. A staff gauge was
established but was discontinued due to sediment build-up. After Day
15, minor inflows from rainfall and pump pond leakage entered the
channel between sample site 10 and 11. This site was sampled for a
total of 88 visits.
12. Pond Effluent -Water quality samples \.Jere taken at four locations to
measure the effect of cifferent effluent filtering methods. All flow
measurements were taken at one location, the Confluence of Pond
Effluents, site nUiri:>er 12A.
12A. QonfJueoce ~ Pond Effluerit3 - A staff gauge was established 300'
below the settling pond and was maintained for the entire sampling
period. Water quality measurements were made next to the staff
gauge.. Water quality mea\sureme~nts were taken for a total of 6
visits. Flow measuremen.ts were taken for a total of 73 visits.
12B. Right OUtlet CUlyert -Water quality samples were collected from
the culvert outlet. The standpipe for this culvert would overflow
only when the trommel was operating. This site was sampled .for a
total of 35 visits.
12C. teft OUtlet CUlvert -Water quality samples were collected from the
culvert outlet. '!he standpi:Pe for this culvert was set lower than
the right culvert standpipe. Therefore this culvert always dis-
charged water. This site was sampled for a total of 31 visits.
12D. Filter .OUtlet CU1vert -Water quality samples were collected from
the culvert outlet. As the filter fabric clogged with silt the
discharge from this culvert decreased. This descrease was deter-
mined by visual estimates. This site was sampled for a total of 18
visits.
13. 5.0.0.!. Downstream -Water quality samples were taken 500' downstream from
the settling pond dam. A staff gauge was established and maintained for
the entire sampling period. There were no additional inflows to the
stream between sample si.tes 12A and 13. The site was sampled for a
total of 89 visits.
...
. 14. 13.l-rpass -For the pump fX'nd used between Day 1 and Day 14, water quality
samples were taken 25' below the effluent of the pond. Flow
measurements were taken at this site. Due to high water conditions, a
staff gauge could not be maintaine<L The sample site was moved when the
pump pond was moved. The new site was on a bypass that carried water
only when the pump rand was full. Flow measurements and water quality
samples from the bypass were taken 10' downstream from the junction of
the pump pond diversion and the bypass. This site was sampled for a
total of 40 visits.
DESCRIPI'ION OF 'WATER QUALI'IY 51\MPLI:tli ME'lliCDS
Method .Qf Collection
Water quality samples were collected at the water surface in one liter
polyethylene bottles, for settleable solids, total suspended solids and
turbidity. Samples to be tested in Fairbanks were ship:p=d in 60, 125,
2~0, 500 or 1000 ml polyethylene sample bottles, depending upon the
amount of sediment.
Dissolyed OXygen, rrg/1
All D.O. measurements were made with a Hach Model16046. Calibration
values were determined each morning and re-determined each afternoon.
The probe was placed approximately 3" below the water surface facing
upstream until a stable reading was reached. This took !~ to 1 minute.
Results were recorded to the nearest 0.1 mg/1.
pH was determined using a ~ Scientific Digital mini-pH meter Model 55.
Standardization was done each morning using 4.0 and 9.0 pH buffers. The
probe was placed approximately 3" below the water surface facing up-
stream until a stable reading was reached. This took approximately 1
minute.. pH values were recorded to the nearest 0.1 pH unit.
Water Tam?erature, ~
All temperature measurements were made with a Taylor field thermometer.
It had a range of -15 to +105°C, graduated in l°C increments. The
thermometer was placed 3" below the water surface. It took approximate-
ly 15 seconds to stabilize before measurements were taken. Temperatures
were read to the nearest 1 degree.
Settleable Solids, mUl
A one liter sample was collected at each sample site to be tested later
in the day using an Imhoff cone. The procedure used is described in
''Standard Methods for the Examination of Water and Wastewater, n 14th
edition, page 95. Results below 0.1 ml/1 were recorded as 0 .. 1 ml/1.
Values between 0.1 and 19.9 w,:re recorded to the nearest 0 .. 1 ml/1.
Results greater than 20 were recorded to the nearest whole number.
I,
Flow,~
All flow measurements were made using a Scientific Instruments pygmy
flow meter Model 1205. The stream cross section was divided into
approximately 20 sectional areas for velocity measurements and area
calculations. Depending on creek conditions, flow values were deter-
mined using one of three methods. The first was actual field measure-
ments using the pygmy flow meter. The second was using a stage-dis-
charge curve determined by actual measurements. The third method was
visual estirnatas based on previous measurements at that site. Flow
measurements were taken at the best channel section nearest the sample
site. Flows less than 10 cfs were recorded to the nearest 0.1 cfs and
values 10 or greater were recorded to the nearest whole number.
Total auapended SOlids, ng/1
Water samples collected at each sample site were shipp:d to Fairbanks
for analysis. '!he procedure used in testing is described in "Standard
Methods for the Examination of Water and Wastewater," 14th edition, page
94.
Turbidity. NW
Water samples collected at each ~ple site were shipped to Fairbru1ks
for analysis. The procedure used in testing is described in "Standard
Methods for the Examination of Water and Wastewater," 14th edition, page
132.
AU. TeiJBrature, ~
All temperature measurements were made with a Taylor field thermometer.
It had a range of -l5°C to +105°C, graduated in l°C increments.
Measurements wer.e made at each site.. The thermometer was hand held
until a stable reading was reached, approximately 1 minute.
Temperatures were read to the nearest 1 degree.
ClQqd Coyer, .1
Percent cloud cover was bar~ on visual inspection of the sky for a full
360°. The thickness of the clouds was not distinguish~
Rainfall, incbes
A rain gauge was installed on flat ground approximately 10' from the
nothwest corner of the tecr~~ician's cabin. The gauge was not shieldea
The gauge was read at 8:00 a.m., noon and at 5:00 p.m. Each time the
gauge was read, it was emptied.
Arsenic, ns/1
Water samples were collected for analysis of dissolved and total arsenic
at the following sites: Above Sluice, Pond Influent and Pond Effluent.
Samples for the dissolved fraction were filtered in the field through
filters having 0.45 micron pore spaces. Analyses were performed at a
l=:tboratory in Fairbanks following 11 Methods for Chemical Analysis of
Water and Waste," 1979, published by the U.S. Environmental Protection
Agency using Method 206.2.
Chanical Ox~en Demand, ns/1
Water samples were collected at high and medium flow conditions and
shipped to Fairbanks for testing. The analytical procedures used are
presented in the u.s. Environmental Protection Agency publication
"Methods for Chemical Analysis of Water and Waste," 1979, Method 410.1
and 410.2.
I u
APPENDIX ZII
" .,,.~ .. ..__ .. ~ ... ,., ..... ~.·"'' ...... -..-... -~.--.--.--..·......llh..,""'""' ... .-, ______ ,.,.._.,_ •>"'•~·-·-~---...... ,
June 26, 1981
Tirne:
Air Temp, oc
Precipitation, inches
Cloud Cover, %
Dissolved Oxygen, mg/1
Temperature, °C
fil, pH Units
Settleable Solids, ml/1
Flow, cfs
TUrbidity, ~mJ
T. Suspended Solids, mg/1
Olem. Oxygen Demand, mg/ 1
Time:
Air Temp, °C
Precipitation, inches
Cloud Cover, %
Dissolved Oxygen, mg/1
Temperature, °C
pi, til Units
Settleable Solids, ml/1
Flow, cfs
Turbidity, NID
T .. SUSJ::ended Solids, mg/1
Chern. Oxygen Demand, ng/1
Time:
Air Temp, °C
Precipitation, inches
Cloud Cover, %
Dissolved Oxygen, m;Vl
Ternp:rature, °C
pH, pH Units
Settleable Solids, ml/1
Flow, cfs
Turbidity, rnu
T. Suspended Solids, mg/1
Chern. OXygen Demand, mg/1
Conments:
DEC DEM:>N.-~TION PRQJECI'
FIELD DA.TA
SAMPLE UX'ATIO~
~ 2. l ~
17:05 17:10 WJ 17:15
17 Dry Sample 17
0 Not 0
90 Taken 90
10.5 12.1
8 9
7.1 7.0
.(0.1 19.0
23 2400
63.8 6250
2 .a ~ lQ.
No No 15:15 15:45
sample sample 16 16
Taken Taken 0 0
90 90.
12.0 11.7
11 10
7.0 7.0
1.0 60
7.0 (E)
800 1400
1490 2830
ll .l4. l.Q. ll
No 15:10 Tr~l WJ
Overflow 16 Not Sample
0 Operat~ng Not
90 Taken
10.2
11
6.6
0.7
650
712
1. CUbic yards moveq/day: Warner: 900-1125; Haskins: 300-375.
Day 1
5_
W'J
Sample
Not
Taken
ll
15:35
16
0
90
12.0
11
6.5
11.0
7 .5 (E)
5300
10000
l2.
~
OVerflow
2.
WJ
Sample
Not
Taken
l2.
No
OVert low
ll
No
OVerflow
2. Equipnent used 9 hours/day: Warner: D-8, 988, D-9/9 hrs; Haskins: D-8, dragline/4 hrs.
3 • Problems: St:r.tong winds slowed operations for both Warner & Haskins.
4. Other Conments :· Warner Clean-up 0700-1200. Flow calculated without tramnel ot;erating.
At settling J:?Ond influent santple site. Warner begins double shift. They hope to sluice
15-18 hrs/day.
j/
DEC DEK>~TION PROJECI'
PIELD mTA
June 28, 1981 Day 2 !'
SAMPLE lOCATION
~ 2. J. .4. 5. .6_
Time: 18:21 19:21 WJ 19:30 WJ Vl.J
Air ;remp, °C 8 6 Sample 6 Sample Sample
Precipitation, inches 0.04 0.04 Not 0.04 Not Not
Cloud Cover, % 75 75 Taken 75 Taken Taken
Dissolved Oxygen, mg/1 11.4 11.0 10.4
Temperature, °C 6 6 6
pH, E;fl Units 7.0 7.1 7.0
Settleable SOlids, ml/1 <.0.1 ~0.1 23
Flow, cfs 16 12
Turbidity, NIU 4.4 24 3700
T. Sus~ed Solids, ~1 8.4 7.9 3440
Olern. Oxygen Demand, mg/1
2 lt ~ lO. ll. l2.(A)
Time: 21:30 21:40 21:15 16:35 16:29 16:20
Air Temp, °C 6 6 6 9 9 9
Precipitation, inches 0.04 0.04 0.04 0.04 0.04 0.04
Cloud Cover, % 75 75 75 90 90 90
Dissolved Oxygen, mg/1 8.5 9.1 9~5 94 9.7 8.5
Temperature, °C 7 7 6 9 9 10
pH, pi units 6.8 6.5 6.8 6.9 6.6 6.8
Settleable Solids, ml/ 1 4:.5 0.7 ~0.1 15.0 16.0 0.1
Flow, cfs 7.0 (E) 7 .5 {E) 5.0 {E)
Turbidity, mu 700 900 1000 1300 2800 1800
T. Suspended Solids, mg/ 1 465 410 635 1090 7460 1460
Clem. Oxygen Demand, ng/1
ll .a J.D. ll ll(A) ll
Time: 16:12 21:10 20:41 21:56 21:05
Air Temp, °C 9 6 Tromnel 6 5 6
Precipitation, inches 0 .. 04 0.04 ~t 0.04 0.04 0 .. 04
Cloud Cover, % 90 75 Operating 75 75 75
Dissolved Oxygen, mg/1 8.6 10.2 9.9 9.4 9 .. 5
Temperature, °C 10 7 5 8 6
pH, pH Units 6.5 6.5 6.3 6 .. 7 6.5
Settleable SOlids, ml/1 0.1 0 .. 1 < 0.1 0.9 0.4
Fl<:M, cfs 0.5 (E)
TUrbidity, NlU 2000 900 1200 5900 2600
T. Sus~nded Solids, ng/1 1200 725 740 5780 2150
Olen. Oxygen Demand, nq/1 -
carments:
1. Cubic yards moved/day: Warner: 1100-1700; Haskins: 700-900.
2. Equipnent used, hours/day: Warner: 944 loader, D-8, D-9/18 hrs.; Haskins: drag1ine,
D-8/9 .5 hours.
3. Problems: Flat tire on loader at 21:00 (Warnet·) o
4. Other Comnents: Settling p:lnd overflowing.
L
DEC .DEMJNSTRATION PRQJECr
FIEID ll\TA
June 29, 1981
Time:
Air Temp, 01 ~
Precioitat.:on, inches
Cloud Cov{;r, %
~
19:31
6
0.04
100
Dissolved Oxygen, mg/1 8 .5
Tanpera.ture, oc 5
pH, pH Units 6.6
Settleable Solids, rnl/1 <. 0.1
Flow, cfs
Turbidity, NTU 5.0
T. Suspended Solids~ rng/1 7.8
Chern. Oxygen Demand, mg/1
•rime:
Air Temp, °C
Precipitation, inches
Cloud Cover, %
Dissolved Oxygen, rng/1
Tem~rature, °C
pH, pH Units
Settleable Solids, mU/1
Flow, cfs
Turbidity, mu
T. Sus~nded Solids, mg/1
Chern. Oxygen Do--mand, mg/1
Time:
Air Temp, °C
Precipitation, inches
Cloud Cover, %
Dissolved Oxygen, rng/1
Temperature, °C
pH, ~ Units
Settleable Solids, ml/1
Flow, cfs
Turbidity, N'lU
T. suspended Solids, m;/1
Chern. Oxygen Demand, rng/1
Comnents:
2
15:45
8
0
75
8.3
7
6.9
3 .. 5
25
650
564
ll
09:48
8
0
60
9.4
8
6.0
{. 0.1
1.6
1900
1460
2.
19:42
6
0.04
100
8.0
5
6 .. 6
<0.1
6.0
6.6
.a
14:50
9
0
75
9.2
8
6.6
0.6
21
800
778
ll
10:35
10
0
60
11.2
6
6.8
0.1
450
354
SZ\MPLE LOCATION
~ .4.
~~
Sample
Not
Taken
.2.
10:45
10
0
60
8.5
8
6.7
0.1
340
314
.lQ.
18:20
6
0 .. 04
100
8.5
8
6.4
5.0
7 .0 (E)
1300
1200
20:00
6
0.04
100
8.1
6
6.7
20
12(E)
4200
5270
J.D.
13:45
7
0
75
9.3
8
7.4
9.0
7.0
1300
2330
ll
18:31
6
0.04
100
7.7
7
6.3
31
7.5 (E)
6900
11500
1. Cubic yards moved/day: Warner: 1100-17001 Haskins: 600-750.
Day3
.i
WJ
Sample
Not
Taken
ll.
12:45
7
0
75
8.6
9
6 •. 2
23
7.4
2700
8210
l2.(A)
18:39
6
0.04
100
7.8
8
6.2
0.4
5.0(E)
2000
1870
2.. Equipnent used,. hours/day: Warner: D-9, 944 loader/18 brs.1 Haskins: Dragline,
D-8/8 hrs.
3. Problems:
.6.
WJ
Sample
Not
Taken
l2JA)
10:25
13
0
60
10.6
8
6.2
<0.1
2400
1750
.ll
18:46
6
0 .. 04
100
7.0
8
6.2
0.1
1800
1560
4 • other Corrurents ~ warners plan on mining down on claim 5 below in approximately 3 0 days.
This might interfere with acquiring the needed 50 sample days.
June 30 , 1981
Time:
Air Temp, °C
Precipitation, inches
Cloud Cover, %
Dissolved Oxygen, ng/1
TEmperature, °C
pH, til Units
Settleable Solids, m.Vl
Flow,~ cfs
TUrbidity, N1U
T. Suspended Solids, m;v'l
Chan. oxygen Demand, mg/1
Time:
Air Temp, oc
Precipitation, inches
O.oud Cover, %
Dissolved Oxygen, mg/1
Temperature, °C
pi, til Units
Settleable Solids, mVl
Flow, cfs
Turbidity, Nru
T. Suspended Solids, mg/ 1
Cllem. OXygen Demand, ng,/1
Time:
Air Temp, °C
Precipitation, inches
Cloud Cover, %
Dissolved Oxygen, ~1
Temperature, °C
Iii, pH Units
Settleable Solids, ml/1
Flow, cfs
Turbiai ty, mu
T. Susp~:nded SOlids, ng,/1
Clem. Oxygen Demand, mg/1
Comnents:
DEC DEK>NSTRATION PROJECT
FIEID Di\TA
l
1.2~38
8
0.02
100
9 .. 3
6
6.9
LO.l
10
6.8
26.2
2
08:24
7
0
90
9.1
5
6.5
0.4
31
16.5
.ll.
10:05
6
0
90
7.9
7
6.2
~0.1
1.6
9§0
584
2.
13:25
8
0.02
100
9.0
6
6.6
<::0.1
15
16
18.6
B.
08:35
7
0
90
9.4
5
6.9
0.3
170
171
li.
10:17
7
0
90
9.3
6
6.6
1.0
18
360
304
SAMPLE IJJCATION
l J.
WJ
Sample
Not
Taken
.2.
10:25
7
0
90
8.8
6
6.9
0.1
320
178
l.Q.
16:20
8
0.02
100
9.3
8
6.4
0.4
7.0{E)
180
1900
20:15
5
0.25
100
8.5
5
6.3
16.0
12
1900
3300
lQ.
10:43
7
0
90
9.6
6
6.5
32
7.0 (E)
2200
1610
16:10
8
0.02
100
8.8
8
6.2
41
7.5 (E)
3800
2790
1. Cubic yards moved/day: warner: 900-1000 J Haskins: 700-900
Day4
WJ
Sample
Not
Taken
ll
10:32
7
0
90
9.0
7
6.4
13.5
7 .5 (E)
1700
600
l2.(A)
16:00
8
0.02
100
9.2
8
6.2
0.1
6 .. 5
1000
396
.6.
WJ
Sample
Not
Taken
l2.{A)
09:06
6
0
90
8.0
7
6.2
<O.l
1.4
1100
508
ll
14:53
8
0.02
100
8.7
9
6 .. 4
0.4
950
564
2. Equipnent used, hours/day: Warner: D-8, D-9/10 hrs. ~ Haskins: dragline, D-8/9.5 hrs ..
3. Problems: Warner1? 944 and 988 loaders broken dcWI' .. The D-8 is p1shing pa.y dirt
into the slick plate.
4. other Cooments: Warner: cleanup fran 0700-1000. Haskins total sluice hours for June
= 31 hours (Day 1-4). Warners total sluice hours for June= 55 hours {Day 1-4).
........ ~¥· ,. ...... ~ • ..-.-.~~-... ·--· ---rl
f ' DEC DEMJNSI'RATION PRQJECr
FIELD DA.TA
July 1, 1981 DayS
I -SAMPLE lOCATION '
' ' l 2. .l J. .5. .2.
Time: 08:40 08:30 WJ 08:16 WJ WJ
r ~ Air Temp, oc 8 8 Sample 8 Sample Sample
Precipitation, inches 0 0 Not 0 Not Not
Cloud Cover, % 80 80 Taken 80 Taken Taken
I ;
I
F Dissolved Oxygen, rrg/1 11.6 11.2 11.9
Tanperature, oc 4 5 5
pH, ~I Units 6.4 6.5 6.4
f ·I Settleable Solids, ml/1 ~0.1 <0.1 16.5 I
Flow, cfs 15(E) 18(E) 12{E)
Turbidity, NIU 5.4 5 .. 8 2200
''· T. Sus~nded Solids, m:Vl 12.8 11.8 1580
Olem. Oxygen Demand, rng/1
' . I .a .2. l.Q. ll. ll(D)
Time: 09:07 09:20 13:58 10:55 10:44 10:34
Air Temp, . °C 9 9 8 10 10 10
Precipitation, inches 0 0 0 0 0 0
Cloud Cover, % 70 70 75 75 75 75
Dissolved Oxygen, mg/1 11.0 11.0 9.0 11.2 10.5 9.8
Temperature, °C 4 4 8 ,. 8 6 0
pH, pH Units 6.6 6.6 6.6 6.1 6.1 5.3
settleable Solids, n0/l 7.0 1.5 o.8 31 16.5 <.0 .1
Flow, cfs 7.0 (E) 7.5 (E) 1.3
Turbidity, NlU 2000 700 500 1900 3600 2600
T. Suspended Solids, mg/1 2440 440 408 2870 3290 1600
Cllern. Oxygen Denand, mg/1
l.l li JJl. ll. l2.(C) J.l
Time: 09:50 10:30 19:14 14:09 13:49 13:39
Air Temp, °C 10 9 6 8 8 9
Precipitation, inches 0 0 0.21 0 0 0
Cloud Cover, % 75 75 100 60 60 60
Dissolved Oxygen, m;/1 10.3 10.8 11.0 10.4 10.5 9o9
Temperature, °C 6 5 6 8 7 8
pH, pH Units 6.0 6.8 6.2 6.2 6.1 6.3
Settleable SOlids, ml/ 1 <0.1 2.0 38 11.0 0.5 0.6
Flow, cfs 3.4 7 .. 0 (E) 7.5 (E) 6.5
Turbidity, mu 800 1000 2900 2100 1900 1400
T. Suspended Solids, ng/1 444 716 1170 870 1140 1010
' Chern. Oxygen Demand, mg/1
l..·
Corrrnents:
1. Cubic yards rnoveQ/day: warner: 1450-1600; Haskins: 500-600.
I, 2. Equi,tnent used, hours/day: Warner: D-8, 988/16 hrs.; Haskins: dragline, D-8/6.5 hrs.
3. Problems: Tronrrel broke down for 1 hour.
4. Other Comnents:
....
July 2, 1981
Time:
Air Temp, °C
Precipitation, inches
Cloud Cover, %
Dissolved Oxygen, mg/1
Tanperature, °C
};fi, pH Units
Settleable Solids, ml/1
Flow, cfs
Turbidity, N1tJ
T. Suspended Solids, rrg/1
Chern. Oxygen Demand, mg/1
Time:
Air Tanp, °C
Precipitation, inches
Cloud Cover, %
Dissolved Oxygen, mg/1
Temperature, °C
pH, I;ii Units
Settleable Solids, ml/1
Flaw, cfs
Turbidity, NlU
T. Suspended Solids, mg,/1
Clem. Oxygen Demand, Itg/1
Time:
Air Temp, ot.:;
Precipitation,, inches
Cloud Cover, ~
Dissolved Oxygen, m;/1
Tenperature,-9 C
pi, pH Units
Settleable SOlids, ml/1
Flew, cfs
Turbidity, N'1U
•
T. Suspended SOlids, ng/1
Olem. Oxygen Demand, mg/1
Corrrtents:
DEC DEK>NSIRATION PROJECT
FIEID MTA
l
09:10
2
0.12
100
13.3
1
6.1
0.6
26
22
51
1
07:35
3
0.12
100
13.0
1
6.0
8.0
550
680
97
ll
09:55
2
0.12
100
12.4
2
6.5
0.4
650
200
110
2.
09:00
2
0.12
100
13.3
1
6.0
2.0
80
74
67 .a
15:15
1
0.22
100
11.7
0
6.0
0.2
650
805
65
.1!
10:10
2
0.12
100
13.0
2
6.0
2.5
340
270
92
SAMPLE ux;ATION
3. .4.
WJ
Sample
Not
Taken
.2.
Pmlp
Pond
Draining
lO.
TrOilliOOl
Not
~rating
08:40
2
0.12
100
13.5
1
6.0
12.5
12(E)
2600
3070
270
l!l
Trarmel
Not
Operating
ll
15:30
1
0.22
100
10.6
2
5.6
2.0
13
160
530
89
1. CUbic yards moved/day: warner: 900-1125; Haskins: 150-200.
Day 6
5.
WJ
Sample
Not
Taken
ll
10:40
2
0.12
100
13.5
1
5.2
20
170
155
89
ll{D)
14:00
2
0.22
100
11.9
1
5.6
0.2
12
900
410
100
.2.
W'J
Sample
Not
Taken
12.( B}
10:17
2
0.12
100
12.3
2
5.6
0.2
600
285
85
ll
Flooded
out By
Pump
Pond
2. Equipnent used, hour1'3/day: Warner: 944 loader, D-8, D-9/9 hr.s1 Haskins: drag1ine.,
D-8/2 hrs.
3.. Problems: Tramel dc'J\m almost all day -problens with the recycle pump.
4. other Coornents: Flood conditions all over, flew impossible to measure at most
sites. CDD sample taken for high flow. Haskins draining their pump p:lro. Discharge
flocx1ing the 500 1 below sample site. WJ sample taken 200 1 below at sample site 13.
Warner cleanup and carmencenent of moving the sluice box, pipes, etc. upstream.
• f
l
·!
f
i
j
j
• I
nEC DEK>NSl'R.l\TION PRClJECI'
FIEID DA.TA
Day7 July 3, 1981
SAMPLE LOCATION
l 2. l J.
Time:
Air Temp, oc
Precipitation, inches
Cloud Cover, %
08:10
1
0.01
100
08:20
0
0 .. 01
100
Dissolved Oxygen, rng/1 12.6 12.5
Temperature, °C
pH, pH Units 6.3 6.3
Settleable Solids, ml/1 ,0.1 <.0.1
Flow, cfs
Turbidity, NIU 10 6.0
T. Suspended Solids, mg/1 4.0 5.6
Chern. Oxygen Demand, mg,/1
Time:
Air Temp, °C
Precipitation, inches
Cloud Cover, %
]_
09:30
1
0.01
100
Dissolved cr~gen, rng/1 12.2
Temperature, °C
pH, pH Units 6.5
Settleable Solids, rnJ/1 1.0
Flow, cfs
Turbidity, NTU 65
T. Suspended Solids, mg/1 640
Chern. Oxygen Demand, rng/1
Time:
Air Temp, °C
Precipitation, inches
Cloud Cover, %
ll
10:25
3
0.01
100
Dissolved Oxygen, ID:3/l 12.5
Temperature, °C
pH, pH Units 5.4
Settleable SOlids, mJ/1 l..O.l
Flow, cfs
Turbidity, NIU 60
T.·Suspended Solids, mg/1 40
Chern. Oxygen Demand, mg/1
Conments:
.a.
09:40
3
0.01
100
12.4
6.1
0.8
170
240
l.i
10:22
3
0.01
100
12.4
6.0
3.7
250
313
1. Cubic yards movedVday: Warner: 0; Haskins: 0
WJ
Sample
Not
Taken
~
10:36
3
0.01
100
11•5
6.1
1.0
160
180
lO.
Trorranel
Not
Operating
2. Equipnent used, hours/day: N:> one sluiced today.
3. Problems:
Not WJ
Sluicing Sample
Not
Taken
l.O.
Trc:mtel
Not
Operating
ll
15:13
10
0
100
11.2
5.5
20
13
ll
10:50
3
0.01
100
12.1
5.5
1.5
120
100
ll(B)
15:00
10
0
100
11.1
5.2
t..O.l
1.5
45
42
~
WJ
Sample
Not
Taken
ll(C)
10:15
3
0.01
100
12.8
5.1
(0.1
50
26
ll
14:55
10
0
100
11.9
5.6
40.1
50
45
4. other O:>mments: Haskins draining their pump J:X>nd. Discharge flooding the 500' below
sample site. WQ sample taken 2 jQ' below at sample site 13. ·
July 6, 1981
DEC DEM:>NSr.RATION PRQJECT
FIEID DA.TA
Day 8
SAMPLE UJCATION
Time:
Air Temp, °C
Precipitation, inches
Cloud Cover, %
~
20:30
6
0
40
Dissolved Oxygen, nq/1 12 .2
Temperature, °C 5
pH, pH Units 6.5
Settleable Solids, ml/1 J.. 0 .1
Flow, cfs
Turbidity, N'lU 1'
T. Susp!nded Solids, mg/1 7.8
Chern. Oxygen Demal'xl, mg/1
Time:
Air Temp, °C
Precipitation, inches
Cloud Cover, %
2
18:35
8
0
50
Dissolved Oxygen, ~1 9.2
Temperature, °C 6
pH, Pi Units 6.1
Settleable Solids, mJ/1 0 .1
Flow, cfs
TUrbidity, NTU 100
T. Suspended Solids, mg/1 95.0
Clem. Oxygen Demand, ng/1
Time~
Air Temp, °C
Precipitation, inches
Cloud Cover, %
Dissolved Oxygen, mg/1
Temperature, °C
Iii, pH Units
Settleable SOlids, ml/1
Flow, cfs
Turbidity, Nl'U
T. Suspended Solids, Rk31'1
Chen. Oxygen DEmand, rrg,l+
Comnents:
ll
16:52
9
0
50
11.7
8
5.8
1.0
2900
1160
2.
Dry
.8.
18:28
8
0
50
10.4
8
6.5
0.1
80
145
li
19:20
7
0
30
11.4
7
6.3
40.1
160
165 -
.l J.
WJ
Sample
~t
Taken
i
19:13
8
0
30
10.6
8
6.4
{0.1
130
90.0
lQ.
18:58
7
0
30
11.8
7
6.2
50
550
160
Not WJ
Sluicing Sample
lO.
16:38
8
0
so
12 .. 2
8
5 .. 9
9.5
900
400
ll
19:05
7
0
30
11.1
7
6.0
2000
4720
Not
Taken
ll
16:31
8
0
so
11.8
8
5.6
14.0
3400
4140
l2.{C)
19:36
8
0
30
11.2
8
5.9
0.8
3400
1240
1. Cubic yards moved/day: Warner: 0; Haskins: 825-1025.
2. Equipnent used, hours/day: Warner: 0~ Haskins: drag1ine, D-8, 983/11 hrs.
3. Problems:
.6..
WJ.
Sample
Not
Taken
l2.(B)
16:4S
8
0
so
11.8
7
5.9
0.5
2200
1690
ll
19:26
7
0
30
11.6
7
6.0
0.9
400
2470
4. Other Carments: Warner nearly finished with moving the sluice box, setting pipes
and canpleting the water pond &mi.
f -
l ' DEC DEMJNSTRATION PRQJECI'
FIEID DA.TA
-.~LilY 7; 1981
SAMPLE I.DCATION
Time:
Air Temp, oc
Precipitation, inches
Cloud Cover r %
~
13:00
6
0.05
100
Dissolved o.x-ygen, mg/1 11 (lo
Temperature, °C 5
pa, pH Units 6.6
settleable Solids, mJ/1 <. 0.1
Flow, cfs 19
TUrbidity, N'ID 2 .6
T. suspended Solids, mg/1 3 0)9
Chan. Oxygen Demand, rnr;Vl
Time:
Air Temp, oc
Precipitation, inches
Cloud Cover, %
Dissolved Oxygen, mg/1
Temperature, °C
pi, pH Units
·ettleable Solids, ml/1
.&:'low, cfs
Turbidity, NTU
T. Susp:nded Solidsr ng/1
Chern. Oxygen Demand, mg/1
Time:
Air Tenp, °C
Precipitation, inches
Cloud Cover, %
Dissolved Oxygen, rng/1
Temperature, °C
pH, pH Units
Settleable Solids, ml/1
Flow, cfs
'I'urbidi ty, NlU
T. Suspended SOlids, mg/1
Chem. Oxygen Demand, mg/1
Comments:
]_
WJ
Sample
Not
Taken1
Warner
Is Not
Sluicing
ll
10:20
8
0.05
100
10.5
7
5.9 < 0.1
1600
1050
2.
Dry
.a
WJ
Sample
Not
Taken,
Warner
Is Not
Sluicing
l.4.
10:44
8
0.05
100
11.0
6
6.1
1.5
600
405
J. .i
WJ
Sample
Not
Taken
3.
10:50
7
0.05
100
10.3
6
6.2
0.1
500
332
lQ.
Tramne1
Not
~rating
Not
Sluicing
lO.
14:20
7
0.05
100
12.0
6
6.4
14.0
5.7
2500
2830
ll
Wj
Sample
Not
Taken,
Trornmel
Not
Operat1ng
1. Cubic yards moveQ/day: Warner: 0; Haskins~ 675-850.
Day9
.5.
Wj
Sample
Not
Taken
ll
14:30
7 o.os
100
11.4
7
6.2
25
3000
5770
l2,{B)
].4:40
7
0.05
75
11.6
7
5.8
0.5
2400
1610
.2.
W,J
Sample
Not
Taken
l2.(D)
10:42
8
0.05
100
11.4
r: .....
2000
),090
ll
14:50
8
0.05
75
10.3
7
6.0
0.8
2200
940
. 2. Equipnent used, hourS/day: Haskins: Dragline, D-88, 988/9 hrs.
' -3.. Problems: Most of the joints in the pipe that feeds Warner's sluice burst. Water
pond had to be drained to repair it.
l .
4. other C.QITUlents: Warner probably will not be sluicing tmtil Thursday by the time
... hey repar the pipes. Flcrw into P..ask:lns pump pond essentially clean water.
l
i
i
i
!
t·
.:
j \
1 ··'
DEC DEMJNS'mATION PRQJECl'
FIEW Di\TA
' ' July 8, 1981 Day 10 '
SAMPUj IDCATIQN
~ 2. l .4. .5. ~
Time: 16:45 Dry ~ ~t WJ WJ
Air 'rE!q;), ° C sample Sluicing Samplt~ Sample
Precipitatioo, inches 0 .. 20 Not Not Not
Cloud Cover, % 100 Taken Taken Taken
Dissolved Oxygen, ng/1
~rature, oc
pi, pH Units
Settleable SOlids, ml/1 ~0 .. 1
Flow, cfs
Turbidity, NI\J 4.6
T. Suspended Solids, mg/1
Chern. Oxygen Demand, mg/1
9.1
2 .a s. JJL ll. J.2.(C)
Time: WJ W'J 15:17 Trcmnel 1\Q 10:40
Air Temp, °C Sample Banple Not Sample
Precipitation, inches Not Not Oe20 Oferating Not 0.09
Cloud Cover, % Taken Taken 100 Taken 100
Dissolved Oxygen, mg/1
~rature, °C
};1i, };ii Uni.ts
Settleabl~ Solids, ml/1 0.6 <-0.1
FlCN, cfs
'1\u:bidi ty, NIU 450 :aoo
T.' Suspended Solids, mg/1 190 930
l ) Olen. Oxygen Demand., rrg/1
13. a lO. ll. l2.(B) ll
Time: 10:30 15:12 16:25 16:15 16:00 15:30
, Air Temp, °C ; ' Precipitatioo, inches 0.09 0.20 0.20 0.20 0.20 0.20
Cloud COVer, % 100 100 100 100 100 100
Dissolved Oxygen, mg,/1 11.0
~rature, °C
I=Hr ~Units 5.5
Settleable Solids, ml/1 0.4 1.0 18.0 26 0.8 1.5
Flow, cfs -21 7.0 (E) 6.3 6 ~o (E)
Turbidity, N.l'U l900 500 5200 8000 2200 1900
T. Suspended Solids, mg,/1 1070 265 928D 16500 1240 1380
Clem. Oxygen Demand, nq/1
Catments:
,. 1. Cubic yards moved/day: Warner: 01Haskins: 675-850.
i ' Ek)uipnent used, hours/day: Haskins: Dragline, D-8, 988/9 hrs. 2.
J ... Problems: 00 and PI meters malfunctioning; broke thennaneter$ Warner w/crushed
t.-
pipe, drained pone.
4. other Carments: Haskins cleaned up one sluice box this morning.
,, DEC DEMJNmRATION PROJEcr
FIEID Dl\TA 1
July 9, 1981 Da:y 11 I
1 SAMPLE IDC'ATION !
l 2. .l i. 5. .2.
Time: 19:36 Dry WJ Not WJ w:2
Air Temp, oc Sample Sluicing Sample Sample
Precipitation, inches 0.02 NOt Not Not
Cloud Cover, % 100 Taken Taken Taken
Dis sol ve<l Oxygen, mg/1
Temperature, °C
pH, pH Units 6.8
Settleable Solids, ml/1 <{0.1
Flow, cfs
TUrbidity, N'lU 5.4
T. Suspended Solids, mg/1 8.6
Chan. Oxygen Demand, mg/1
1 .a .9. lQ. ll l2.{D)
Time: WJ WJ 10:44 11:00 10:25 10:35
Air Temp, oc Sample Sample
Precipitation, inches Not Not 0 0 0 0
Cloud Cover, % Taken Taken 50 60 50 50
Dissolved Oxygen, mg/1
Temperature, °C
pH, J:;ii Units 6.4 6.2 6.2 6.1
Settleable Solids, ml/1 0 .. 2 64 16.0 {0 .1
Flow, cfs 7 .0\E) 9.5 (E)
f ~· Turbidity, NIU 45 8900 3800 2100
T. Suspended Solids, mg/1 44.0 30700 5830 1290
Chern. OXygen Demand, rrg/1
' ll l4. .lQ. ll ll(B} ll I -~·'
Time: 10~48 10:39 15:27 15:19 15:07 14:35
Air Temp, °C
Precipitation, inches 0 0 0.02 0.02 0 .. 02 0.,02
t ·-· f Cloud Cover, % 50 50 100 100 100 100
Dissolved Oxygen, mg/1
Temperature, °C
I;f{, pH Units 6.2 6.4 5.9 6.1 6.0 6,4
Settleable Solids, ml/1 0.1 3.5 70 44 1.5 0.7
Flow, cfs 7 .O{E) 9.5 6>1'7
Turbidity, NIU 1700 140 10600 6200 2600 2500
T. Suspended Solids, rng/1 1210 179 25900 7790 1840 1660
Chern. Oxygen Demand, mg/1
Comments:
la Cubic yards moved/day: Warner: 0; Haskins: 700-900.
2. Equipment used, hour$/day: Haskins: Dragline, D-8, 988/9.5 hrs.
C .... 3. Problans:
4. Other Cat!Irents: Warner acquired the pipe needed from Dave Underwood.
{_ .;.:
\
\ -
DEC DEMJNSTRATION PRQJECl'
FIEID DA.TA
July 10, 1981
~IDeATION
Time:
Air Temp, oc
Precipitation, inches
Cloud Cover, %
Dissolved Oxygen, mg/1
Temperature, °C
~
15:10
0
100
};ii, pH Units 6.4
Settleable Solids, ml/1 <.0 .1
Flow, cfs 36
Turbidity, NTU 7.4
T. Sus~nded Solids, ma_./1 3 .2
Clem .. Oxygen Demand, mg/1
Time:
Air Temp, °C
Precipitation, inches
Cloud Cover, %
Dissolved OXygen, rng/1
Temperature, °C
2
10:15
0
100
pH, pH units 6.4
Settleable Sol ids, ml/ 1 0 .1
Flow, cfs 35
Turbi~ity, NTU 30
To Sust-~nded Solids, mg/1 25
Clem. OX}"gen Demand, mg/1 -
Time:
Air Temp, °C
Precipitation, inches
Cloud Cover, %
Dissolved Oxygen, mg/1
Temperature, °C
ll
14:10
0
100
I1'Ir pH Units 6 .. 3
Settleable Solids, ml/1 0 .. 8
Flow, cf~ -
TulJ~lidity, N'IU 2200
T. Suspended Solids, ng,/1 1830
Clem. Oxygen Demand, mg/1 •\<
Ccmnents:
2.
Dry
.a
10:55
0
100
6.2
~0.1
37
36
36
l!
14:33
0
100
6.5
<O.l
70
66
.l .i
WJ
Sample
Not
Taken
.2.
14:28
0
100
-·
6.4
<0.1
flO
80
10.
18:49
0.1
100
61
7.0 (E)
10600
22000
Not
Sluicing
JJl
13:35
0
100
6.3
57
7.0 (E)
7500
15000
ll.
18:54
0.1
100
23
S .5 (E)
7500
7170
1. CUbic yards moved/day: Warner: 0; Haskins: 825-1050;;
2. P.quipnent t!sed, hours/day: Haskins: Dragline, D-8, 988/11 hrs.
3. Problems: pH meter broke in the afternoon.
4 • Other Corrrnents:
Day 12
5.
WJ
Sample
Not
Taken
ll.
13:28
Q
100
6.1
42
9.5 (E)
6600
14500
l.2.(B)
19:06
0_.1
100
1.0
... ,oo· . .: ~
~870
WJ
Sample
Not
Taken
l2.{C)
14:21
0
100
6.0
0.6
1900
1840
ll
19:01
0.1
100
1.0
3800
2660
l
j
I ~ DEC DEM>NSI'RATION PRQJEcr
FIELD DA.TA
July 11, 1981 Day 13
SAMPLE lOCATION
l. 2. J. J. .5. .6.
Time: 16:40 Dry WJ Not ~ WJ
Air Temp, oc Sample Sluicing Sample Sample
Precipitation,-inches 0.09 Not Not Not
Cloud COver, % 100 Taken Taken Taken
Dissolved Oxygenf mg/1 I,
Temperature, °C
J_:if, £if Units 6.8
Settleable Solids,. ml/1 ~0.1
Flaw, cfs 37(E)
TUrbidity, Nru 3.4
T. Sust:ended Solids, mg/1 0.1
OJ.ern. Oxygen Demand, mg/1
2 B. .2. lQ ll ll(D)
Time: 10:53 12:51 14:24 10:32 10:53 10:36
Air Temp, oc
Precipitation, inches 0.09 0.09 Oo09 0.21 0.21 0.21
Cloud Cover, % 100 100 100 100 100 100
Dissolved Oxygen, mg/1
Tempeit'ature, °C
pH, pH Units 6.4 6.6 6 .. 5 6.0 6.0 5.7
3ettleable Solide, ml/1 1.0 ~0.1 1.5 0.2 24 1.5
Flow, cfs 7.0 (E) 9.5 (E)
Turbidity, NIU 5800 400 500 3100 5800 2600
T. Suspended Solids, mg/1 7390 38 .. 0 158 4990 7390 990
Chern. Oxygen Demand, rng/1
ll li. l!t ll. ll{C) ll
Time: 10~32 13~21 14:40 14:48 14:17 14:05
ld.r Temp~ °C
Precipitation, inches 0.21 0.09 0.09 0.09 0.09 0.09
Cloud Cover, % 100 100 100 100 100 100
Dissolved Oxygen, rng/1
Temperature, °C
J.:*I, pH Units 6.0 6.4 6.1 '1.9 5.8 6.0
Settleable Solids, inl/1 0.2 0.1 13.0 24 0.3 1.0
Flow, cfs 28 5.6 9.5 6.7
Turbidity, NTU 1900 110 1800 6700 3100 3400
T. Suspended Solids, mg/1 870 44.0 1730 6320 2860 1990
Clem. Oxygen Demand, mg/1
{ -
Comments:
1. Cub.: .. c yards moved/day: Warner: 0; Haskins: 825-1050.
2. Equipment used, hour~day: Haskins: Dragline, D-8, 988/11 hrs.
' \.,._, 3~ Problems:
4. other Comrrents: Haskins plan on moving upstream approximately 400' to a new mine cut
within a tew days.
l_,.
!
DEC DEMJNSTRATION PROJECr
FIEID Dt\TA
July 12, 1981 Day 14
SAMPLE I.QC'ATION
l 2. J. j_ .5. .6.
Time~ 12:52 13:01 WJ 14:09 Vl.J W,)
Air Temp, °C Sample Sample Sample
Precipitation, inches 0 0 Not 0 Not Not
Cloud Cover, % 50 50 Taken 50 Taken Taken
Dissolved Oxygen, mg/1
TemJ:."Erature, °C
pH, pH Units 6.6 6 .. 5 6.1
Settleable SOlids, ml/1 <:..0.1 <O.l 8.5
Flow, cfs 34{E) 16 14
Turbidity, N'IU 14 7.4 2300
T. Suspended Solids, rng/1 20.8 2.2 1770
Clem. Oxygen Demand, mg/1
]_ .a .2. lO. ll l2.(B)
Time: 10:03 10:00 10:37 10:47 10:42 10:32
PJ.ir Temp, °C
Precipitation, inches 0 0 0 0 0 0
Cloud Cover, % 75 75 75 75 75 75
Dissolved Oxygen, rng/1
Temperature, °C
pH, pH Units 6.5 6.4 6.5 5.7 5.6 5.7
Settleable Solids, ml/1 3.0 1.5 0.5 90 48 1.0
Flow, cfs 7 .0 (E) 9.5 (E)
Turbidity, :mu 800 650 650 11800 1200 4600
T. Suspended Solids, mg/1 900 410 250 1000 880 4380
Olem. Oxygen Demand, mg/1
ll li. lO. ll ll(D) ll
Time: 10:26 10:21 16:15 16:09 15:40 14.:58
Air Temp, °C
Precipitation, inches 0 0 0 0 0 0
Cloud Cover, % 75 75 60 60 60 60
Dissolved Oxygen, mg/1
Temperature, °C
pH, pH Units 6.0 6.5 5.7 6.1 5.8 5.8
Settleable Solids, ml/1 0.7 0.2 27 18.0 1.0 2.0
Flow, cfs 7.0 {E) 9.5 {E) 6.0 5.0
Turbidity, mu 3400 200 7200 3900 7500 5400
T. Suspended Solids, mg/1 2600 120 15000 4200 9380 4560
Clem. Oxygen Danand, mg,/1
Comments: j
1. CUbic yards moveQ/day: Warner: 500-625; Haskins: 800-1000. l
2. Equipment used, hour~day: Haskins: D-8, drag1ine, 988/10.5 hrs; Warner: D-9r 988/5 hrs.
3. Problems:
4. Other Canments: Haskins plans on moving Monday. Flow at sample site 2 includes
~"--~ estimated flow from dam and pipe leaks (5.0 cfs).
t .. ·.
-
DEC DFX>NSTRATION PROJEcr
FIElD IY\TA
July 18, 1981
SAMPLE I.DCATION
Time:
Air Temp, oc
Precipitation, inches
Cloud Cover, %
Dissolved Oxygen, mg/1
Temperature, °C
pH, pH Units
Settleable Solids, ml/1
Flow, cfs
Turbidity, t-m:J
T. SusJ;Ended Solids, mg/1
Chern. Oxygen Demand, mg/1
Time:
Air Temp, °C
Precipitation, inches
Cloud Cover, %
Dfssol ved Oxygen, mg/ 1
Ten)I)erature, °C
pH,· pH Units
Settleable Solids, ml/1
Flow, cfs
Turbidity, mu
T. Suspended Solids, rng/1
Chern. Oxygen Demand, mg/ 1
Time:
Air Temp, °C
Precipitation, inches
Cloud Cover, %
Dissolved Oxygen, mg/1
Temperature, °C
pH, pH Units
Settleable SOlids, ml/1
Flow, cfs
Turbidity, NIU
T. Suspended Solids, ng/1
Chern. Oxygen Demand, rng/1
Coourents:
l.
13:26
18
0.03
90
10.6
10
6.4
<..0 .. 1
6.9\
3.2
1.5
1
w:J
Sample
Not
Taken
ll
16:26
22
0.03
75
10.3
13
6.2.
(0.1
2.0(E)
550
345
2. J.
Dry WJ
Sample
Not
~ken
Ji i
w.2 No
sample Recycle
Not Water
Taken
~4. 10.
~ Troti'ClOO 1
Sample Not
Not Operating
'1aJten -"'.
1. Cubic yards moved/day: Warner: 800-1000; Haskins: 0
2. Equipnent used, hours/day: Warner: D-8,988/8 hrs
3. Problems:
.4.
14:23
20
0.03
90
10.8
10
6.2 s.s
13(E)
1600
2370
lQ.
Tranmel
Not
Operating
ll
WJ
Sample
Not
Taken
Day 15
.5. ;~
V.Q \\Q
Sample Sample
Not Not
Taken Taken
ll ll(B)
15:07 16:10
20 21
0.03 0.03
90 90
10.1 10.4
13 12
6.{) 6 .. 1
(0.1 <.O .1
0.4 (E) 1.4 (E)
110
190
l2. ll
WJ W;J
Sample Sample
Not Not
Taken Taken
4. other COmrrents: Porcupine CreE;k flow reduced 75\'t from 7/12. Nearly 100 ft. of the
settling J;X>nd influent end is filled in with sedi.m:!nt. Haskins new pump p::>nd not
built yet, therefore no recycle water.
f •
( .
,,
( .
DEC DEfwDNS.mATION PRQJEcr
FIELD DATA
July 19, 1981
SAMPLE IDC.ATION
l 2. 3..
Time: 10:00 Dry WJ
Air Temp, °C 14 Sample
Precipitation, inches 0 Not
Cloud Cover, % 75 Taken
Dissolved Oxygen, mg/1 10.4
Temperature, °C 9
pH, pH Units 6.5
Settleable Solids, ml/1 <.0.1
Flow, cfs 8.0 (E)
Turbidity, NTU 3.6
T. Sus:penoed Solids, mg/1 5.8
Chern. Oxygen Demand, mg/1
1 .a .9.
Time: WJ WJ No
Air Temp, °C Sample Sample Recycle
Precipitation, inches Not Not Water
Cloud Cover, % Taken Taken
Dissolved Oxygen, mg/1
Temperature, °C
pH, pH Units
Settleable Solids, ml/1
Flow, cf.s
Turbidi t:y, mu
T. SUSl?ended Solids, mg/1
Chern. Oxygen Demand, rng/1
ll li. lQ.
Time: 13:51 rtJ Tremmel
Air Temp)' °C 15 Sample Not
Precipitation17 inches 0 ~t Operating
Cloud Cover, % 75 Taken
Dissolved Oxygen, ng/1 9.3
Temperaturt~, °C 13
pH, pH Units 6.3
Settleable SOlids, rnl/1 <.0.1
Flow, cfs 0.4
Turbidity, mu 3500
T. Suspended Solids, mg/1 240
Chern. Oxygen. .Demand, mg/1
Corrments:
1. Cubic yards moved/day: Warner: 600-750; Haskins: 0
2.. Equipnent used, hours/day: Warner: D-9,988/6 hrs
J.
Not
Sluicing
.10.
Tranmel
Not
Operating
ll
WJ
Sample
Not
Taken
Day 16
.5.. .6..
WJ 15:17
Sample 15
Not 0
Taken 75
9.1
12
6 .. 1
< 0.1
<O.l(E}
200
215
ll l2.(C)
15:55 14:20
14 15
0 0
50 50
9.2 9.5
12 12
5.7 6.1
2.0 (0.1
1.3 0.8
160 320
1550 340
l2. ll
WJ WJ
Sample Sample
Not Not
Taken Taken
3. Problems: Warner: D-8,944 broken down. Not enough water to ~~luice more than 6 hrs.
4. Other Conments: Warner clean-up. Warner water pond cut in half to eliminate two
major leaks~~
DEC DEftDNS['AATION PROJEcr
FIEW MTA
July 20, 19 81 Day 17
SAMPLE IDCATION
~ 2. .l .4. .5. .2.
Time: 19:20 Dry ~ Not WJ 14:40
Air Temp, °C 11 Sample Sluicing Sample 18
Precipitation, inches 0 Not Not 0
Cloud Cover, % 75 Taken Taken 75
Dissolved Oxygen, rrg/1 10.8 9.5
Temperature, °C 10 11
pH, pH Units 6.7 6.2
Settleable Solids, ml/1 <0.1 40.1
Flow, cfs 7.1 0.5
TUrbidity, l-.1TU 4.4 200
T. Suspended Solids, rrg/1 5.5 480
Cllem. Oxygen Demand, m9/l
2 .a .9.. JJl ll l2.(D)
Time: WJ WJ No Tramrel 13:37 14:25
Air Tanp, °C Sample Sample Recycle Not 18 18
Precipitation, inches Not Not Water Operating 0 0
Cloud Cover, % Taken Taken 75 75
Dissolved Oxygen, mg/1 9.4 9.5
Temperature, °C 15 12
pH, pH Units 6.0 6.1
3ettleable Solids, rnl/1 "0 .1 < 0.1
Flow, cfs 1.3 {E)
Turbidity, .Nru 60
T. Suspended Solids, mg/1 405
Chern. Oxygen Demand, mg/1
ll l.4. JJl ll. .l2.
Time: 14:00 h"Q Trcmnel WJ w:2
Air Temp, °C 18 &mtple Not Sample Sample
Precipitation, inches 0 Not Of;erating Not Not
Cloud Cover, % 75 Taken Taken Taken
Dissolved Oxygen, rng/1 9.6
Temperature, °C 14
pH, pH Units 6.0
Settleable Solids, ml/1 <0.1
r"'low, cfs 0.4
Turbidity, NID 190
T. Suspended Solids, ~1 560
Chern. Oxygen Demand, mg/1
Comments:
1. Cubic yards moveq/day: Warner: 100-125; Haskins~ 0
2. Equipment used, hours/day: Warner: D-9,988/1 hr.
3.. Problems: Not enough water to sluice more than 6 hrs. straight. 988 broke down.
4. Other camnents: Not taking WJ samples at sample sites 10, 11, 12, 13 twice/day
since Haskins hasn't sluiced in 8 days. Warner stripping down on claim 5 below.
0.8
400
650
ll
~
Sample
Not
Taken
DEC DEM>NSI'RATION PRQJECl'
FIELD CATA
July 21, 1981
SAMPLE LOCATION
Time:
Air Temp, °C
Precipitation, inches
Cloud cove~, %
Dissolved Oxyg·en, mg/1
Temperature, °C
pH, pH Units
Settleable Solids, ml/1
Flow, cfs
Turbidity, NTU
T. Suspended S()lids, mg/1
Olen. Oxygen Demand, mg/1
Time;
Air Temp, °C
Precipi tati,:>n, inches
Cloud Cover, %
Dissolved <Ar;ygen, mg/1
Temperature, °C
pH, pH Units
Settleable Sol.i.ds, ml/1
Flow, cfs
Turbidity, N1U
T. Suspended SOlids, mg/1
Clem. Oxygen Demant1, mg/1
Time:
Air Temp, °C
Precipitation, inches
Cloud Cover, %
Dissolved Oxygen, mg/1
Temperature, °C
pH, pH Urdts
Settleable Solids, rnl/l
Flow, cfs
Turbidity, N'IU
T. Suspended Solids, mg/1
Chern. Oxygen Demand, mg/1
Camnents:
~ 2.
18:30 Dry
14
0
90
10.4
9
6.4
(0.1
6.0 (E)
1.8
7.2
1. .a
w:J w:l
sample Sample
Not Not
Taken 'Taken
ll li
13:54 w:.l
16 Sample
0 Not
60 Taken
10.0
13
6.0
0.6
0.3 (E)
850
1100
1. Cubic yards moved/day: Warner & Haskins: 0
2. Equipnent used, hours/day:
l .4.
WJ Not
sample Sluicing
Not
Taken
.9. lO.
No Tranmel
Recycle Not
Water Op:!rating
l.O. ll
Tronmel WJ
Not Sample
Operating Not
Taken
Day 18
.5.
W'J
Sample
Not
Taken
.ll
16:05
18
0
60
9.7
14
6.2
<0 .. 1
1$0 (E)
100
590
12.
WJ
Sample
Not
Taken
3 • Problans: Warner does not have equipnent available. They have all broken down ..
4. Other Corrments: WJ sample for 200 • bel~ contaminated •r~i th test hole washings.
' •. ,,_ --~·-----.. ____,..._._:;
~
W'J
Sample
Not
Taken
l2.{C)
14:10
18
0
60
10.4
12
6.2
(0 .. 1
0.5 (E)
500
420
ll
~
Sample
Not
Taken
DEC DEM:>NSTRATION PR<lJ~cr
FIEID MTA
JUlY 22, 1981 Day 19
SAMPLE LOCATIOB
~ 2. ~ .4. 5. ~ I
I
Time: 12:50 Dry WJ 14:01 WJ 16:00 :
Air Temp, oc 18 Sample 18 sample 17
Precipitation, inches 0 Not 0 Not 0.,01
J
Cloud Cover, % 50 Taken 75 Taken 100
Dissolved Oxygen, mg/1 10.6 11 .. 4 9.8
Temperature, 0 e 9 12 13
I pH, pH Units 6 .. 5 6 .. 4 6.4
Settleable Solids, ml/1 <.0.1 24 0.1
Flow, cfs 4.9 12 -
Turbidity, NIU 7 .. 0 1500 550
T. suspended Solids, mg/1 16 3300 530
Chan. Oxygen Demand, mg/1
1 .a Q
.-!. lQ. ll l2.{B)
Time: WJ WJ No Trorranel 15:00 15:45
Air Temp, °C Bample sample Recycle Not 18 17
Precipitation, inches Not Not Water O{:erating 0.01 0.01
Cloud Cover, % Taken Taken 100 100
Dissolved Oxygen, mg/1 9.5 10.4
Temperature, °C 12 14
pH, Iii Units 5.9 6.1
·ettleable Solids, ml/1 7.5 0.2
t'low, cfs 18{E) 15(E)
Turbidity, NIU 900 600
T. suspended Solids, mg/1 1390 640
Chern. Oxygen Demand~ ng/1
ll l! lQ. ll l2. ll
Time: 16:20 ~ Trornmel WJ w.:l W'J
Air Temp, oc 17 Sample Not Sample Sample sample
Precipitation, inches 0.01 Not Operating Not Not Not
Cloud Cover, % 100 Taken Taken Taken Taken
Dissolved O~gen, rng/1 10.3
Temperature, °C 14
pH, pH UnitS 6;,2
Settleable Solids, ml/1 1.0
Flow, cfs 15(E)
Turbidity, N'ID 350
T. Suspended Solids, mg/1 960
Che11. Oxygen Demandy mg/1 .,.
COmments:
1. Cubic yards moveq/day: Warner: 300-375; Haskins:O.
2. Equipnent used, h<..,urs/day: Warner: D-9 ,988/J hrs.
3. Problems: Haskins has trouble holding water in their new pUlllp pond due to tailings.
J?robably delay sluicing for a few days more. Warner cannot sluict.~ more than 5 hour~
due to low water.
-4 Other canments: •
DEC DEmNS"mATION PROJECt'
FIEID ~TA
July 23, 1981 Day 20
~· .t)JCATION
l 2. ~ ! .5_ .6.
Time: 13·~05 Dry WJ 12~45 WJ 15:25
Air Temp, °C 12 Sample 12 Sample 11
Precipitation, inches 1.5 !i:>t 1.5 Not 1.5
Cloud Cover, % 100 Taken 100 Taken 100
Dissolved Oxygen 1 mg/1 11.8 9.8 10.7
Temperature, °C 10 10 12
pH, fH Units 6.9 6.4 6.2
Settleable Solids, m]/1 -'0.1 26.0 0.2
Flow, cfs 8.5 (E) lO.O(E) <.O.l(E)
Turbidity, N.ru 20 3100 600
T. Suspended Solids, mg/1
Chern. OXygen Dei;!land, m:J,./1
29.0 5350 760
2 .a i l.Q. ll J.2.(B)
Time: W.l WJ No Tramnel 15:50 15:23
Air Temo °C -, Sample Sample Recycle Not 11 11
Precipitation, inches Not Not Water Operating 1.5 1.5
Cloud Cover, % Taken Taken 100 100
Dissolved OXygen, mg/1 10.8 ll.l
Temperature, °C 10 11
pH, pH Units 6.2 6.0
Settleable Solids, ml/1 0.3 <. 0.1
Flow, cfs 2. 0 {E) 2.7
Turbidity, Nru 800 600 ~ T. SUSJ,:ended Solids, mg/1 480 880 .I Chern. OXygen Demand, mg/1
ll li lO. ll l2. ll
Time: 14:00 ~ Trommel w:l WJ vJJ
Air Temp, °C 11 Sample Not Sample Sample Sample
Precipitation, inches 1.5 Not Operating Not Not Not
Cloud Cover, % 100 Taken Taken Taken Taken
Dissolved Oxygen, mg/1 10.6
Temperature, °C 11
pH, pH Units 6.3 ' Settleable Solids, ml/1 !0.1 j
Flow, cfs 2.3 i ~ Turbidity, NlU 500
T. Suspended Solids, rng/1 550
Chern·. Oxygen Demand, mg/1
Con'ments:
1. Cubic yards moved/day: Warner: 300-375. Haskins: 0.
2. Equipnent used, hours/ day: Warner: D-9, 944/5 hrs.
3. Problems:
4. Other COmments: Creek water level on the rise. This should increase sluice hours.
July 24, 1981
Time:
Air Tenp, oc
Precipitation, inches
Cloud Cover, %
oisso1 ved Oxygen, mg/1
Temperature, °C
pi, ~ Units
Settleable Solids, ml/1
Flow, cfs
TUrbidity, Nlt1
T. Suspended Solids, m:y'l
Chern. Oxygen Demand, mg/1
Time:
Air Temp, °C
Precipitation, inches
Cloud Cover, %
Dissolved Oxygen, mg/1
Temperature, °C
pH, pH Units
Settleable Solids, ml/1
Flow, cfs
Turbidity, mu
T .. Suspended Solids, rng/1
Chern. Oxygen Danand, ng/1
Time:
Air Temp, °C
Precipitation, inches
Cloud Cover, %
Dissolved Oxygen, mg/1
Temperature, °C
pfl, pH Units
Settleable Solids, ml/1
Flow, cfs
Turbidity, N'IU
T. Suspended Solids, nq/1
Chan. Oxygen Demand, mg/1
Ccm'oonts:
DEC D~TION PRQJECI'
FIELD MTA
l
10:36
23
0
30
11.2
9
6.6
40.1
22.0
50
95.5
2
w;J
Sample
Not
Taken
ll
15:01
23
0
50
10.8
13
6.5
0~4
lO(E)
850
630
2.
10:25
23
0
30
11.1
10
6.3
<0.1
13.0
18
10.0
.a
~
Sample
Not
Taken
li
12:35
25
0
40
10.4
12
7 .. 0
0.4
12(E)
320
300
SAMPLE lOCATION
·3. .4.
WJ
Sample
Not
Taken
S!.
12:48
25
0
40
10.8
14
6 .. 7
< 0.1
550
255
ln.
Trommel
Not
Operating
09:50
23
0
30
11.2
9
6.5
11.0
9.1
1500
4450
ln.
13:00
25
0
40
11.0
10
6.0
85
7.6
7700
14700
ll
WJ
Sample
Not
Taken
1. CUbic yards moved/day: Warner: 500-625; Haskins: 500-600.
Day 21
.5.
WJ
Sample
Not
Taken
ll
13:40
24
0
50
10.3
12
6.1
13.0
12
2300
1930
ll
WJ
Sample
Not
Taken
\c')
Sample
Not
Taken
ll(B)
14:30
23
0
50
10.8
12
6.3
0.4
12
2100
1250
ll
WJ
Sample
Not
Taken
2. Equipnent used, hours/day: Warner: D-8, 988/5 nrs; Haskins: dragline, D-8/6.5 hrs.
3 • Problet'lS:
4. Other Camnents: Haskins sluicing for the first time since Day 14.
•
DEC DEMJNS".LRATION PROJECr
FIEID DM'A
July 25, 1981 Day 22
SAMPLE LOCATION
~ .2. .l .4. 5. .6.
Time: 16:01 16:11 WJ 16:18 w.J 14:17
Air Temp, °C 17 17 sample 17 Sample 20
Precipitation, inches 0 0 &:>t 0 Not 0
Cloud Cover, % 75 75 Taken 75 Taken 75
Dissolved Oxygen, mg/1 11.9 11.6 13.3 10.5
Tanperature, oc 10 10 10 12
pi, pH Units
Settleable Solids, rnl/1 <.0.1 <.O.l 29 1.0
Flow, cfs 17 (E) 2.5 (E) 9.0(E) <.O.l(E)
Turbidity, Nru 110 40 7200 1900
T. Suspended Solids, mg/1 125 44.0 10700 1850
Chern. .. Oxygen De!rra"'ld, mg/1
1 .a .9. l.O.. ll l2.(D)
Time: WJ ~ 12:55 13:01 13:40 14:39
Air Temp, °C Sample Sample 20 20 20 20
Precipitation, inches Not Not 0 0 0 0
Cloud Cover, % Taken Taken 75 75 75 75
Dissolved Oxygen, mg/1 9.9 12.3 11.6 10.6
'Ienperature, oc 12 11 12 10
pH, pH Units
Settleable Solids, ml/1 0.5 100 10.0 1.5
Flow, cfs 6.8 12 7.9
Turbidity, NltJ 600 11800 3300 1500
T. Suspended Solids, mg/1 490 41400 3360 1930
Chern. Oxygen Demand, rrg/1
ll u. 1.0. ll l2. ll
Time: 15:15 12:45 Trorranel WJ W'J WJ
Air Temp, °C 20 20 Not Sample Sample Sample
Precipitation, inches 0 0 Operating Not Not Not
Cloud Cover, % 75 75 Taken Taken Taken
Dissolved Oxygen, mg/1 11.2 11.9
Temperature, °C 13 12
til, pH !.!nits
Settleable Solids, ml/1 0.3 3.5
Flow, cfs 5.7 12(E)
Turbidity, NTU 1600 550
T. Suspended Solids, ng/1 1570 335 1
Chern. Oxygen Demand, mg/1 .
Canments: ~
1. CUbic yards moveq(day: Warner: 1500-1875; Haskins: 675-850.
2. Equipnen.t used, hourS/day: Warner: D-8, 988/15 hrs.; Haskins: Dragline, D-8, 988/9 hrs.
3. Problems:
4. other Catanents: Trammel broke down in the afternoon so no second samples were taken.
DEC DE.PrDNS'J.'RATION PROJECT
FIET.D MTA
JulY 26, 1981 Day 23
~.ux;ATION
l 2. l .i .5. .2.
Time: 13:30 Dry Wj Not 13:15 WJ
,rJ.r '1\:!nP, o c 15 Sam:ole Sluicing 15 Sample
Precipitation, inches 0 Not 0 Not
Cloud cover, % 30 Taken 60 Taken
oissol ved Oxygen, mg/1 11.3 11.8
Tanperature, oc 12 13
p1, Iii Units . o.a settleable So1~ds, ml/1 (. 0.1
Flow, cfs 8.5 (E) 3.0 (E)
rurbidi ty, N'1U 1200 20
T. suspended SolidsH rrg/1 910 53.0
Qlem. OXygen Demand, mg/1 49 10
1 .a 3. ~ ll l2.(B)
Time: WJ WJ 10:34 10:42 10:48 10:22
Air •remp, oc Sample Sample 17 17 17 16
Precipitation, inches Not Not 0 0 0 0
Cloud Cover, % Taken 'Taken 30 30 30 30
Dis:5o1 ved Oxygen, mg/ 1 9.2 11.7 11.1 11.2
Temperature, ()c 12 12 12 12
pH, pH Units
Settleable Solids, ml/1 0 .. 1 83 9.0 ~0.1
Flow, cfs 7.0 (E) 10.0 (E) 4.0{E)
Turbidity, mu 650 5800 16U0 2800
T. Suspended SOlids, mg/1 660 4630 2770 670
01em.. Oxygen Demand, ng/1 26 620 180 58
ll l:1 J.D. ll ll(C) ll
Time: 10:11 10:29 14:05 14:48 15:13 15:45
Air Temp, °C 15 17 16 16 15 15
Precipitation, inches 0 0 0 0 0 0
Cloud Cover r ~s 30 30 60 60 60 60
Dissolved Q<-..(}'gen, mg,/1 10.8 10.9 11.1 10.8 12.2 11.5
Tenperature, °C 12 13 13 12 13 14
I=Hr pH Units
Settleable Solids, ml/1 l_O.l 1.5 3.0 10.0 0.4 0 .. 5
Flcrt¥, cfs 4.0(E) 7.0 (E) 6.6 10 12 6.7
'1\lrbidity, NID 1900 75 400 2800 3000 1400
T. Sus~nded Solids, ng/1 790 114 620 3900 1470 1290
Clem. Ox-ygen Demand, mg/1. 56 15
Corrments:
1. Cubic yards moved/day: Ha.r;kins: 675-850; Warner:O.
2. F.quipnent used, hour.t"/dc.-y: Ha~*ins: drag1ins, D-8, 988/9 hrs.
3. P.r.ob1ans: Warner: 988 brcke down again.
4. Other Ccmnents: <DD sample taken at nooerate flow level. Warner cleanup.
DEC DEM)NSI'RATION PRQJECI'
FIEID Ill\TA
July 27, 1981
Time:
Air Temp, oc
Precipitation, inches
Cloud Cover, %
~
13:23
21
0
75
Dissolved OXygen, mg/1 11.3
Temperature, °C 12
J;fl, pH Units
Settleable Solids, mJ/1 0 .5
Flow, cfs 8.9
Turbidity, NID 900
T. Suspended So1idst rna_/1 620
Clem. Oxygen Demand, mg/1
Time:
Air Temp, °C
Precipitation, inches
Cloud Cover, %
Dissolved Oxygen, mq/1
Temperature, °C
pH, :til Units
Settleable Solids, ml/1
Flaw, cfs
Turbidity, mu
T. Suspended SOlids, mg/1
Olem. Oxygen Demand, mg/l
Time:
Air Te:np, oc
Precipitation, inches
Cloud Cover, %
Dissolved Oxygen; mg/1
Temperature, · °C
pi, pH Units
Settleable SOlids, ml/1
Flow, cfs
Turbidity, NTU
T. Suspended Solids, mg/1
Chern. Oxygen Demand, mg,/1
Conrnents:
2
WJ
Sample
Not
Taken
ll
10:37
18
0
75
10.5
18
(0.,1
2.5(E)
650
220
2.
14:09
20
0
75
10.7
12
(0.1
1.0 (E)
70
50.0
.a
W2
sample
Not
Taken
l!
10:52
18
0
75
10.7
14
0.6
1.5(E)
650
310
SAMPLE LOCATION
3.. .4.
WJ
Sample
Not
Taken
~
10:55
18
0
75
9.7
13
{0.1
650
410
.lO.
15:34
17
0
75
11.8
13
18.0
7.7
3000
1390
14:00
20
0
75
11.8
11
16.5
ll.O(E)
2600
5090
JJl
11:02
18
p
75
11.3
12
51
7 .O(E)
5600
11200
ll
14:40
17
0
75
11.3
13
6.5
9.5
2000
1540
1. Cubic yards moved/day: Warner: 1500-1875; Haskins: 675-85.0.
Day 24
.5.
WJ
Sample
Not
Taken
ll
11:09
18
0
75
10.8
13
16
lO(E)
3100
4690
ll(B)
16:48
18
0
75
11.7
14
0.4
7.9
1900
1110
.6.
15:57
18
0
75
10.7
13
0 .. 8
<. 0.1 (E)
1600
1400
ll_(D)
10:45
18
0
75
9.7
11
( 0.1
3 .S(E)
500
190
ll
16:06
18
0
75
11.3
14
0.2
9.7
1500
1150
2. Equi~nt used, hours/day: Warner: D---8, 988/15 hrs; Haskins: dragline,I>-8, 9t!8/9 brs.
3. Prob1ans:
4. other Carments: Both operations running smoothly.
.•
I
f • .
DEC DFJt'DNSTRATION PRQJECT I
!
FIEID Df\TA I .
July 28, 1981 I
Day 25 .
SAMPLE IDCATION
~ 2. 3. .4. 5.. 2.
Time: 13:17 Dry WJ Warner WJ 15:35
Air Temp, oc 20 Sample Not Sample 18
Precipitation, inches 0 Not Sluicing Not 0
Cloud Cover, % 75 Taken Taken 75
Dissolved Oxygen, rng/1 12.3 10.5
Temperature, oc 12 13
pH, pH Units
Settleable Solids, rnJ/1 0.6 t. 0.1
Flow, cfs 7.5 (E) <.O.l(E)
Turbidity, NW 650 l400
T. Suspended Solids, mg/1
Olem. Oxygen Demand, mg/1
860 670
]_ .a .2. JJL ll ll(C)
Time: WJ WJ 10:49 Tratmel 10:55 10:36
Air Temp, oc Sample Sample 22 r.bt 21 22
Precipitation, inches Not Not 0 O};erating 0 0
Cloud Cover, % Taken Taken 40 40 40
Dissolved Oxygen, mg/1 9.4 11 .. 6 12.4
Temperature, °C 12 12 12
pH, pH Units
Settleable Solids, rnl/ 1 40.1 0.9 ~0.1
Flow, cfs 2.8 (E) 2.2 (E)
Turbidity, NlU 700 550 700
T. Sus:pended Solids, mg/1 390 650 290
Chern. Oxygen Demand, rng/1
ll li 10.. ll ll(B) ll
Time: 10:26 10:44 Trormnel 15:41 15:30 14:25
Air Temp, °C 19 22 Not 19 18 18
Precipitation, inches 0 0 Operatir19 0 0 0
Cloud Cover! % 40 40 75 75 75
Dissolved Oxygen, rng/1 11.3 12.1 10.9 11.1 11.7
Tem_perature, °C 13 11 12 13 13
pHI! pH Units
Settleable SOlids, ml/1 t.O.l 1.5 0.3 <.0.1 <0.1
Flow, cfs 2.3 1.8(E} 2.8 2.2 2.1
Turbidity, N1U 950 1000 550 800 800
T~ susp:nded Solids, m]/1 410 1410 290 10400 390
Chern. Oxygen Demand, rng/1
Conments:
1. CUbic yards moved/day: Warner: 500-625; Haskins: 0
2. F.quipnent used, hours/day: Warner: D-8,988/5 hrs.
3. Problens: Trorrrne1 down all day.
4. Other camrents: warner clean-up in the afternoon. Night shift moving the sluice
box 150' toward the dam. Sluicing set for 'nlurs 7/30: ~ve down on claim 5 belCM by 8/5/81.
DEC DEM:>NSIRATION PROJECI'
FIEID I.lf\TA
,July .29, 1981 Day 26
SAMPLE lOCATION
l. 2. .l !. 5. .6.
Time: 14:20 14:31 WJ Not w:l WJ
Air Tern;_:.:, °C 12 10 Sample Sluicing Sample Sample
Precipitation.~ inches 1 1 Not Not Not
Cloud Cover, % 100 100 Taken Taken Taken
Dissolved Oxygen, ng/1 11 .. 3 10.4
Temperature, °C 10 10
pi, pH Units
Settleab1~ Solids, ml/1 0.4 (. 0.1
Flow, cfs 4.9 6.0
Turbidity, N1tJ 500 360
T. Suspended Solids, mg/1 340 1030
Chern. Oxygen Demand, mg/1
ll l2.(D) 2 .a. ~ lO.
Time.: WJ WJ 12:51 Tremmel 13:05 13:40
Air Temp, °C sample Sample 14 ~t 14 14
Precipitation, inches Not Not 0 Operating 0 0
Cloud Cover, % Taken Taken 50 60 60 .
Dissolved Oxygen, mg/1 11.3 12.2 10.0
Temperature, °C 12 12 11
pH,· pH Units
Settleable Solids, ml/1 ~0 .. 1 (0.1 '0.1
Flow, cfs 2.8 2.2
Turbidity, Nru 550 280 650
T. Suspended Solids, rng,/1 250 197 180
Chern. Oxygen Demand, rrg/1
ll li. JJl ll ll(C) ll
Time: 14:00 12:45 16:00 16:25 16:33 16:41
Air Temp, °C 12 14 11 12 12 12
Precipitation, inches 1 0 1 1 1 1
Cloud Cover, % 100 50 100 100 75 75
Disso1 ved Oxygen, rng/1 10.5 10.6 11.3 10.8 11.5 11 .. 2
Temperature, °C 12 13 12 11 12 12
Pit pH Units
Settleable Solids, ml/1 40.1 2.5 72 9.0 <:.0.1 0.1
Flow, cfs 2.1 8.0 {E) 7.4 10.0 (E) 7.5 (E) 8.6
Turbidity, N.ru 500 190 7200 1800 700 800.
T. SusJ;ended Solids, rng/1 220 237 13300 2490 340 340
Chem. Oxygen Demand, mg/1
Comments:
1. CUbic yards moved/day: Warner: 0; Haskins: 375-470.
2. Equipnent used, hours/day: Haskins: dragline, D-8, 988/5 hrs.
3. Problens: Haskins has sane welding to do on the trorrmel; repair leaks in pipe.
4. Other Contnents: Warne~ still in the process of tooving.
I
DEC DEM>Ns.mATION PROJECI'
FIEID DA.TA
July 29, 1981 Day 26
SAMPLE IDCATION
l. 2. .l J. 5. .6.
Time: 14:20 14:31 WJ Not w:! WJ
Air Temp, °C 12 10 Sample Sluicing Sample Sample
Precipitation, inches 1 1 Not Not Not
Cloud Cover, % 100 100 Taken Taken Taken
Dissolved Oxygen, m;/1 11.3 10.4
Temperature, °C 10 10
p:I, pH Units
settleable Solids, ml/1 0.4 ~0.1
Flow, cfs 4.9 6.0
Turbidity, NlU 500 360
T. Suspended Solids, mg/1 340 1030
Chen. Oxygen Demand, m9/l :
2 .a ~ JJl ll ll(D)
I Time: WJ V(2 12:51 Tranmel 13:05 13:40
Air Temp, oc sample Sample 14 '&>t 14 14
Precipitation;o inches Not Not 0 Operating 0 0
Cloud Cover, % Taken Taken 50 60 60
Dissolved Oxygen, mg/1 11.3 12.2 10 .. 0
Temperature, °C 12 12 11
pH, pH units
Settleable Solids, ml/1 ~0.1 {0.1 <.. 0.1
Flow, cfs 2.8 2.2
Turbidity, Nru 550 280 650
T. Suspended Solids, mg,/1 250 197 180
Chern. Oxygen Demand, mg/1
ll Jj_ lQ. ll. l2.(C) ll
Time: 14:00 12:45 16:00 16:25 16:33 16:41
Air Temp, °C 12 14 11 12 12 12
Precipitation, inches 1 0 1 1 1 1
Cloud Cover, % 100 50 100 lOO 75 75
Dissolved Oxygen, mg/1 10.5 10.6 11.3 10.8 11.5 11.2
Tenperature, °C 12 13 12 11 12 12
til, pH Units
Settleable Solids, m.l/1 t.O.l 2.5 72 9.0 .(.0.1 0.1
Flow, cfs 2.1 8.0 {E) 7.4 lO.O(E) 7.5 (E) 8.6
Turbidity, NTU 500 190 7200 1800 700 800.
T. Suspended Solids, ng/1 220 237 13300 2490 340 340
Chern. Oxygen Demand, mg/1
Comments:
1. CUbic yards moved/day: Warner: 0; Haskins: 375-470 ..
2. Equipnent used, hours/day: Haskins~ drag line, D-8, 988/5 hrs.
3. Problans: Haskins has sane welding to do on the tronmel; repair leaks in pi~.
4. Other Conments: Warner still in the process of 100ving.
tJ
(J
t:. 1'1
July 30, 1981
'time:
Air Temp, oc
Precipitation, inches
Cloud Cover, %
Dissolved Oxygen, rng/1
Temperature, °C
fii, pH Units
Settleable Solids, rna;1
Flow, cfs
Turbidity, mtJ
T. suspended Solids, mg/1
Chan. Oxygen Demand, mg/1
Time:
Air Temp, oc
Precipitation, inches
Cloud Cover, %
Dis~olved Oxygen, mg/1
Temperature, °C
pH, :til Units
Settleable Solids, ml/1
Flow, cfs
Turbidity, NIU
T. Suspended Solids, mg/1
Clem. Oxygen Demand, mg/1
Time:
Air Temp, °C
Precipitation, inches
Cloud Cover, %
Dissolved Oxygen, rrg/1
Temperature, °C
pi, pH Units
Settleable Solids, rnl/1
Flow, cfs
Turbidity, NTU
T. Suspended Solids, ng/1
Cbem. Oxygen Denand, m;/1
Corrments:
DEC DEMJNSTRATION PRQJECI'
FIEID MTA
l
12:49
10
0.6
100
12.6
10
~0.1
4.9
75
151
2
~
Sample
Not
Taken
ll
10:40
11
0
100
12.0
10
<.0.1
2.0 (E)
450
230
2.
12:59
10
0.6
100
11.0
10
~0.1
1.5
80
58.0
.a
WJ
sample
Not
Taken
l.4.
10:10
11
0
100
11.7
10
0.2
5.0 {E)
95
900
WJ
Sample
Not
Taken
~
10:15
11
0
100
10.4
10
<.0.1
500
210
lO..
16:40
13
0
50
12.2
12
48
7.5 {E)
6200
8460
1. Cubic yards moved/day: Warner: 0; Haskins: 525-650.
2. Equipnent used, hours/day: Haskins: dragline, 988/7 hrs.
3. Problems:
Not
Sluicing
l.Q.
11:00
11
0
100
12.6
10
43
7.5 (E)
7500
17800
ll.
16:03
15
0.6
50
12.1
12
7.5
9.8
800
5330
Day 27
5.
12:42
10
0
100
12.8
9
.(0 .1
1.0 (E)
6.8
8.8
ll
10:47
1.1
0
100
11.4
10
9,,5
lO(E)
2600
1830
ll(B)
14:54
13
0.6
75
12.6
11
1.5
3.5
2100
640
4. other Canments: Warner waiting for their new sluice box to be completed.
~
~
Sample
Not
Taken
l2.(D)
10:24
11
0
100
10.9
10
<0.1
2.2
850
520
ll
13:55
12
0.6
75
12.4
ll
1.5
4.4
850
380
DEC DEM>NSTRATION PRQJECT
FIEID Dl\TA
July 31, 1981 Day 28
SAMPLE U?CATION
~ 2. J. ! 5. .2.
Time: 15:50 16:00 WJ Warner w:J 15:12 Air Temp, °C 13 12 Sample Not Sample i3 ~ Precipitation, inches 0 0 Not Sluicing Not 0 f Cloud Cover, % 100 100 Taken Taken 75 t ~ Dissolved Oxygen, ng/1 12.2 10.5 10.8 I
Temperature, °C 10 10 11 f
:ffl, pH Units t .:-j
Settleable Solids, rnl/1 1.5 ~0.1 0.5 t Flow, cfs 4.2 (E) 4.0{E) <.0.1(E)
TUrbidity, Nl.l1 1300 500 1200 i
~ T. Suspended Solids, mg/1 961 283 1230
Chern. Oxygen Demand, mg/1 l 2 .a. ~ .JJl. ll J.2.(C}
Time: ~ J!JJ 12:41 12:35 13:20 15:07
Air Temp, °C Sample Saitple 14 14 14 13
Precipitation, inches Not Not 0 0 0 0
Cloud Cover, % Taken 'l'aken 75 75 75 75
Dissolved Oxygen, mg/1 10.4 11.3 11.0 11.6
Temperature, °C 11 11 12 11
pH, pH Units
Settleable Solids, ml/1 (0.1 61 7 .s 0.1
Flow, cfs 7.6 10 3.0
Turbidity, NlU 110 10800 1400 45
T. Sm;pended SOlids1 mg/1 70 32800 1720 620
Chern. Oxygen Demand, mg/1
ll 1.4. 1.0. ll .J.2.(B} ll
Time: 14:15 12:46 18:41 18:50 19:04 19:15
Air Tenp, °C 13 14 13 13 12 12
Precipitation, inches 0 0 0 0 0 0
Cloud Cover, % 75 75 100 100 100 100
Disso1 ved <YJCYgen, :{~'-..:·J. 11.0 11.2 11.3 11.1 10.9 11.2 . ., ;• 11 Temperaturr~, °C · 11 11 10 12 11
];H, pH Units
Settleable Solids, ml/1 (0.1 0.6 47 5.0 0.2 0.1
Flow, cfs 3.3 2.0 (E) i .5 (E) lO(E) 5.6(E) 4.9
TUrbidity, N'1'U 1200 130 10800 110 1100 1200
T. S~nded Solids, mg/1 680 134 269~0 2220 670 750
Olem. Oxygen Demand, mg/1
Carrnents:
1. CUbic yards moved/day: Warner: 0~ Haskins: 600-750. ·
2e Equipnent used, hours/day: Haskins: dragline, 988/8 hrs.
3. Problems: All of Haskins' cats are broken down.
4. Other Comments: Warner still working on the new sluice box -sluicing possible by
8/2. Haskins total sluice hours for July: 149.5 hrs. (Days 5-28) • Warner total sluice
hours for July: 83 hrs. (Days 5-28) ..
August 1, 1981
Time:
r1 Air Temp, °C
~, Precipitation, inches
Cloud Cover, %
n ~, i Dissolved Oxygen, mg/1
!!>i Temperature, °C
pH, pH Units
11.. Settleable Solids, ml/1
l" Flow, cfs
.J Turbidity, ~"''U
~~ T. Suspended Solids, mg/1
I! Olan. Oxygen Demand, mg/1
~.!
Time:
r;,., Air Temp, ° C U Precipitation,
Cloud Cover, %
inches
F~ i · Dissolved Oxygen, mg/1
l; Temperature, °C
pH, pH Units
t~ ...• ;··~. ~ettleable Solids, rn]/1
~ elow;. cfs
Turbidity, NIU
T. Suspended Solids, rng/1
r[·i Chern. Oxygen Demand, rng/1
-f
Time:
r;•. Air Temp, °C
Precipitation, inches
u Cloud Cover, %
t1.· Dissolved Oxygen, mg,/1
•: Temperature, °C
pH, pH Units
·-· Settleable Solids, ml/1
( Flow, cfs
Turbidity, mu
.,, T. Suspended Solids, mg/1
~, Chan. Oxygen Demand, mg/1
~
Comrrents:
DEC DFIDNSl'RATION PROJECl'
FIEID ~TA
l
14:26
13
0
100
13.4
10
0.9
6.9
800
870
2
W'J
sample
Not
Taken
ll
12:44
14
0
100
12.3
12
(0.1
1.5
600
750
2.
15:00
14
0
100
12.8
11
1.'.0.1
4.0(E)
500
1310
.a
WJ
Sample
Not
Taken
li.
14:14
13
0
100
12.9
12
1.2
6.0
400
610
15:40
14
0
100
13.6
9
t. 0 .l
3.0 (E)
3.0
19
.2.
14:08
13
0
100
11.3
11
(. 0.1
170
1990
10.
Trorranel
Not
Operating
~., 1. Cubic yards moved/day: Warner: 0; Haskins: 0
~· 2. Equipment used, hours/day:
= 3. Problems: Warner~ A gear broke in Haskins dr.agline.
Warner
Not
Sluicing
l.Q.
Tranmel
Not
Operating
ll
20:52
13
0.50
100
10.6
1~
<.O .1
2.4 (E)
90
448
Day 29
5..
i5:10
14
0
100
13.5
12
~0.1
1.0 (E)
14
14
ll.
13:40
14
0
100
12.5
11
0.3
2.4
160
545
ll(C)
20:58
13
0.50
100
11.3
12
~0.1
1.7
650
1070
21:03
13
0.5
100
10.3
12
~0.1
<.O.l(E)
450
920
.l2. (D)
13:30
14
0
100
12.0
10
<. 0.1
1.7
550
370
ll
21:09
13
0.50
100
10.6
11
~0.1
1.4(E)
700
990
4. Oti1er Cotrrnents: Warner: new sluice box should be canpleted by tanorrCM. Warner will
',:~ pr~bably not move down to claim 5 below-will stay near camp. Took late night WJ sample
~ ~Day 29, 30 and 31 for different pond characteristics at sample sites 11, 12 and 13.
[
[
[
l
l
August 2, 1981
Time:
Air Temp, °C
Precipitation, inches
Cloud Cover, %
Dissolved Oxy~en, mg/1
Tenperature, C
pH, pH Units
Settleable Solids, m.l/1
Flow, cfs
Turbidity, NTU
T. Suspended Solids, mg/1
Clem. Oxygen Demand, mg/1
Time:
Air Temp, °C
Precipitation, inches
Cloud Cover, %
Dissolved Oxygen, mg/1
Tenperature, °C
pH, pH tJnits
Settleable Solids, ml/ 1
~,low, cfs
Turbidity, NllJ
T. SUspFAlded SOlids, mg/1
Clem. Oxygen Demand, rrg/1
Ti1t1e:
Air Temp, °C
Precipitation, inches
Clot..td O:>ver: ,. %
Dissolved Oxygen, m:J/1
Tenper~'ture, °C
fti, Iii Units
Settlea!Jle Solids, ml/1
Flow, cfs
Turbidity, NIU
T. Suspended Solids, m:Vl
Chern. Oxygen Demand, ng/1
Colr.Tents:
DEC DEMJNSmATION PROJECT
FIEID MTA
l
15:20
12
0.1
100
11.4
9
1.5
7 .2(E}
600
1060
1
WJ
5anple
Not
Taken
ll
13:30
10
0~1
100
1l.4
11
40.1
1.5
160
490
.2.
14:34
12
0.1
100
10.3
10
~0.1
3 .. 1
65
292
.a
WJ
Sample
Not
Taken
l.4.
12:23.
12
0 .. 1
100
11.2
11
"'~0 .1
3.9
60
356
SAMPLE LOCATION
.l .4.
W,J
Sample
Not
Taken
~
12:28
12
0.1
100
10 .. 5
12
.(0.1
130
490
Warner
Not
Sluicing
lO.
Tratmel
Not
OJ;:erating
lO. ll
'l'rOI\'Ilel 22:49
Not 4
C)J;et:ating 0
0
10.2
9
< 0.1
2 .,4 (E)
80
200
1. Cubic yards moved/day: Warner: 0; Haskins: 0
2. Equi~..nt used, hourS/day:
Day 30
5.
WJ
Sample
Not
Taken
ll
13:06
12
0.1
100
11.1
10
<0.1
2.4 (E)
65
75.0
l2.(D)
23:00
4
0
0
10 .. 1
10
<0.1
1.7
280
345
.6.
13:16
11
0.1
100
10.8
10
~ 0.1
4( 0.1
180
630
ll(B)
13:20
11
0.1
100
11.1
10
<: 0.1
1.7
280
355
ll
22:55
4
0
0
10.4
9
<0.1
1.5
190
840
3. .Problems: Haskins: putting new gear in dragline. Warner: still waiting for their
new sluice box to be completed.
4. Other Ccmnents: Took late night WJ samples on Days 29, 30 and 31 for different
pond characteristics at ~e sites 11, 12 and 13.
j
'1 L,
(
1
,)
r
[
r
DEC DEIDNSTRATION PRQJECJ.1
FIELD IY\TA
August 3, 1981
SM~ IDl;ATION
Time:
Air 'l'emp, oc
Precipitation, inches
Cloud Cover, %
Dissolved Oxygen, my'l
Temperature, oc
pH, pH Units
Settleable Solids, n:J/1
Flow, cfs
TUrbidity, NTU
T. Suspended Solids, ng/1
Chan. Oxygen Denand, mg/1
Time:
Air Temp, oc
Precipitation, inches
Cloud Cover, %
Dissolved Oxygen, mg/1
Temperature, °C
pH, pH Units
Settleable Solids, ml/1
Flow, cfs
Turbidity, NIU
T. Suspended Solids, mg/1
Chern. Oxygen Demand, mg/1
Time:
Air Temp, °C
Precipitation, inches
Cloud Cover, %
Dissolved Oxygen, mg/1
Temperature, oc
pH, pH Units
Settleable Solids, ma/1
b .. low, cf:s
Turbidity, NTU
T. Suspended Solids, ~1
Chern. Oxygen Demand, mg/1
Comments:
l 2.
14:05 13:45
12 12
0 0
10 10
11.6 10.€
8 8
1.0 40.1
8.1 3.8 (E)
650 160
1100 336
]_ .a
WJ WJ
Sample Sample
Not Not
Taken Taken
ll li.
12:30 13:00
11 11
0 0
20 20
11.2 11.4
11 11
40.1 0.8
1.5 5.8 (E)
120 70
355 104
1. Cubic yards moved/day: Warner: 0; Basins: 0
2. Equi~nt used, hours/day:
J. .4..
WJ Not
SC1.mple Sluicing
Not
Taken
.2. .. !"\ .JJ.L
13:20 Trooa--ne1
11 Not
0 Operating
20
11.5
10
(.0.1
100
96.0
lO. ll
Tronmel 22:00
Not 7
Operating 0
0
10~9
8
~ 0.1
2.4(E}
70
72
Day 31
5. .6..
WJ 12:51
~ ..... 1 11 o~e
""'ot · 0 (,~
Taken 20
11))1
10
4G .~1
<0.1
140
450
ll ll(C}
13:21 12:39
11 11
0 0
20 20
11.2 12.1
9 9
< 0.1 <0.1
2~4(E) 1.7
50 360
54 404
ll(B) ll
22:10. 22:18
7 7
0 0
0 0
11.6 11.7
9 9
~0.1 L.O .1
1~7 1.5
100 120
430 430
3. Problems: Haskins: still fixing dragline. Should be sluicing by 8/4 afternoon.
4. Other Comnents: Warner: stripping with the D-9/18 hrs/day on cla:iln 5 below.
Might be sluicing by 8/4 afternoon,. Took late night WJ samples at sites 11, 12 and 13.
[~
~ ... ' ... ! f
')
llj
[
r
[
[
AUgust 4, 1981
Time:
Air Tenp, °C
Precipi tatial, inches
Cloud Cover, %
Disool ved Oxygen, mg/1
Temperature, °C
pi, ~Units
Set~leable Solids, m.l/1
FlO"SJr cfs
TUrl?irlity, mu
T. SU$pended Solids, mg/1
Olen. Oxygen Demanc.l, nq/1
iJ.~:
Ait Temp, oc
Precipitation, inches
Cloud Cover, %
Dissolved Oxygen, rag/1
Tenperature, °C
pi, Iii Units
Settleable Solids, ml/1
Flow, cfs
Turbidity, Nru
T. Sus~ded SOlids, 11¥}1'1
Chern. Oxygen Deland, n.)/1
Time:
Air Tertp, °C
Precipitation, inches
Cloud ~er, %
Dissolved OXygen, mg/1
Temperature, °C
tfl, Iii Units
Settleable SOlids, ml/1
Flow, cfs
Turbidity, NTU
T. Suspended Solids, lD!J/1
Clem. Oxygen Demand, mg/1
Ccmnents:
DEC DF..rOlS'ml\TION PRQJECl'
FIEIDI o.\TA
~
12:23
14
0
0
11.8
9
2.8
7.8
1200
2140
1
WJ
s.ple
Not
Ta.l(en
ll
15:00
14
0
0
11.8
11
0.4
9.2
850
1110
SAMPLE IOCATJ:ON
2. .l .4.
10:33
12
0
0
10.2
8
1.8
4.2
180
512
.a.
W'J
sanpl.e
Not
Taken
JJ.
13~26
14
0
0
11.0
12
2.1
1.8
800
920
i(l
sample
t«:>t
Taken
~
13:20
14
0
0
10.6
12
(0.1
140
550
lD.
18:32
14
0
0
11.2
12
35
7.5
6900
12800
!«>t
Sluicing
lQ.
13:15
14
0
0
11.6
9
34
7.7
3700
10600
ll.
18:40
14
0
0
11.4
12
8.0
lO{E)
2900
4090
1. CUbic yards moved/day: Warner: 01 Haskins: 475-600.
Day 32
.5.
WJ
Sample
Not
Taken
ll
14:08
14
0
0
11.2
12
12
10
2800
4490
J.2.(C)
18:50
14
0
0
10.9
12
0.7
8.4
800
1820
2. F.quipnent used, hours/day: Haskins: Dragline, 988 loa.der/6 .5 hrs.
3 • Problenis: Haskins: replaced worn-out sprockets in the trarrrel in the morning.
14:40
14
0
0
10 .. 9
10
0.2
~ 0 .l{E)
ll(D)
14:45
14
0
0
10 .. 6
10
0.8
8.4
3500
1510
ll
18:45
14
0
0
11.6
12
0.8
8.,5(E)
1200
1380
4. Other Ccmnents: Warner: JOOVed their new sluic~ box dan to the mine cut. Should be in
by tanorrow afternoon. ·
[
[
l
l
·~·:
[
1·.
August 5, 1981
DEC D~T.ION PRQJECI'
FIEID DA.TA
SAMPLE. I.OC'ATLOO
Day 33
.5. l
13:05
16
2. .l .4.
Time:
Air Temp, °C
Precipitation, inches
Cloud COver, %
Dissolved Oxygen, rno_/1
Tanperature, °C
-Iii, ~ Units
Settleable Solids, ml/1
Flow, cfs
Turbidity, NTU
T. S~nde;.~ Solids, mg/1
Olen. Oxyger .. Demand, mg/1
Time:
Air Temp, °C
Precipitation, inches
Cloud Cover, %
Dissolved Oxygen, mg/1
Temperature, °C
{:fl, pi Units
Settleable Solids, ml/1
Flow, cfs
Turbidity, Nru
T. Suspended Solids, mg/1
Chan. Oxygen Demand, nq/1
Time:
Air Temp, °C
Precipitation, inches
Cloud Cover, %
Dissolved Oxygen, mg/1
~rature, °C
I=flr pH Units
Settleable Solids, ml/1
Flow, cfs
TUrbidity, NIU
T. suspeooed Solids, ng/1
Clem. Oxygen Danand, mg/1
Conments:
0
10
11.2
9
4.1
6 .S(E)
2200
3770
2
WJ
Sample
Not
Taken
ll
10:33
14
0
10
12.6
12
<: 0.1
1.4
900
1250
12:39
16
0
10
12 .. 5
9
0.1
4.0(E)
160
528
B.
·W'J
sample
Not
Taken
li.
10:53
14
0
10
13.3
11
.t.0.1
6.5 (E)
190
428
13:25
16
0
30
11.8
7
{0.1
5.8(E)
8.0
24 .. 0
9..
10:56
14
0
10
12.1
11
~0.1
700
1340
lO.
14:02
15
0
75
11.8
10
45
7.6
3900
9490
1. Cubic yards moved/day: Warner: 0; Haskins: 450-550.
2. Equipnent used, hours/day: Haskins: Dragline, 988/6 hrs ..
3. Problems:
Not 12:58
Sluicing 16
lQ.
Trarmel
Not
Operating
ll
15:10
15
0
75
9.8
11
14.0
10
3000
3560
0
10
13.3
11
<O.l
1.0(E)
7.8
10.0
ll
11:01
14
0
10
11.9
10
1.8
2 .2(E)
2200
1810
ll(B)
15:46
14
0
75
11.7
12
0.9
8 .. 4
2300
1550
.6.
15:50
14
0
75
10.3
11
2.8
< 0.1 (E)
1900
2240
U(C)
10:43
14
0
10
13.6
10
<O.l
1.8(E)
1200
1570
ll
16:00
14
0
75
l0 .. 7
12
0.7
9.2
1800
2240
4. other Carments: warner new' sluice box in place, waiting for bolts to· finish sluice
box before they can start sluicing.
' ' ~'
''
August 6, 1981
Time:
Air .. Temp, °C
Precipitation, inches
Cloud COVer, %
Dissolved Oxygen~ mg/1
Temperature, °C
fH, pH Units
Settleable Solids, ml/1
Flow, cfs
Turbidity, Nl'U
T. Suspended Solids, mg/1
Clem. Oxygen Demand, mg/1
Time:
Air Temp, °C
Precipitation, inches
Cloud Cover, %
Dissolved Oxygen, mg/1
Temperature, °C
pH, pH Units
Settleable Solids, ml/1
Flow, cfs
Turbidity, NitT
T. Suspended Solids, mg/1
Clem. Oxygen Demand, mg/1
Time:
Air Temp, °C
Precipitation, inches
Cloud COVer, %
Dissolved Oxygen, ~1
Tanperature, °C
pH, pH Units
Settle.able Solids, ml/1
Flow, cfs
'l.Urbidi ty, NTU
T. Suspended Solids, m;/1
Clem. Oxygen Demand, mg/1
Camlents:
DEC DEM:>NSIFATION' PRQJE.'C1'
FIEilD ~TA
l
10:00
15
0
50
12.0
8
1.4
7.5 {E)
500
1330
1
WJ
&np1e
Not
Taken
ll
15:05
19
0
60
12.2
12
0.2
7.8
1400
1820
10:20
16
0
so
10.5
8
<.0.1
3 .,0 (E)
120
369
.a
WJ
Sall\ple
Not
Taken
li.
13:25
20
0
50
12.0
12
0.6
1.1
120
204
~~ I.DCATTON .. . ~
Day 34
5. .l .i
~
Sartple
Nq·t
Taken
~
13:48
19
0
so
10.5
12 -
~0.1
190
420
lO.
18:36
16
0.20
75
13.0
12
125
7 s5 {E)
13:\00
22200
Not w;J
Sluicing Sample
JJl
13:5S
19
0.
50
12.4
11
27
7.2
3400
9300
ll
18:30
16
0.20
75
12 .. 0
12
9.0
lO(E)
2SOO
4940
Not
Taken
ll.
12:SO
17
0
50
11.6
11
7.5
9.6
2300
3860
ll(C)
18:57
16
0.20
75
13 .. 0
11
0.2
8.4
1800
2230
1. Cubic yards movecl,lday: Warner: 0; Haskins: 550-7uO.
2. Equipnent used, hours/day: Haskins: Dragline, 988/7.5 hrs.
3. Problems: Warner repairing D-9, 988. Haskins repairing their old D-8.
14:47
20
0
60
11.7
11
2.0
~O .. l(E)
1300
2410
l2.(D)
14:52
20
0
60
12.1
10
1.3
8.4
2000
2330
ll
18:46
16
0.20
75
12.6
11
0.1
7.H
1300
2450
4. Other COOUnents: By the time Warner cc.n sluice there will be little water since
it hasn•t rained steady in over a week. Haskins preparing slickplate/sluice box for
their other mine cut below Warner.
l 1
[i
:
[ DEC DEMJNSTRATION PRQJECl'
' FIEID MTA
' .-\ugust 7 , 19 81 Day 35
SAMPLE IDCATION
[ l 2. J. .i 5. .6.. ''
·.-: ,,
Time: 09:20 13:52 WJ Not WJ 10:55
r Air Temp, oc 14 16 Sctnple Sluicing Sample 15 :: Precipitation, inches 0 0 Not Not 0
,. Cloud Cover, % 50 100 Taken Taken 50
f' Dissol vea Oxygen, rng/1 10.8 10.s 9.7
[ Temperature, oc 7 10 12 J..,'J
~~ til Units
(' Settleable SOlids, rnl/1 ~0 .. 1 ~0.1 1.0
-·~ Flow, cfs 3.4 1.8 (E) t.O.l(E)
Turbidity, mu 40 60
T. Suspended Solids, ng/1 132 125
[ Chem. OXygen Demand, mg/1
2 .a ~ JJl ll. ll.{B)
Time: WJ WJ 10:35 15:05 14:15 11:02
[' Air Temp, °C Sample Sample 14 17 16 14
~:: Precipitation, inches Not Not 0 0 0 0
Cloud Cover, t Taken 'Iaken 50 100 100 50
f' Dissolved Oxygen, mj/'1 10.3 11.4 10.1 10.2 .
~' Temperature, oc 12 12 12 10
pH, Iii Units
r Settleable Solids, ml/1 <0.1 75 15.0 0.8
Flow, cfs 7.5 10 1.7
~,..o;f/ Turbidity, NIU 140 8600 5100 3300
T. susrended SOlids, mg/1 500 28200 7840 2330
~· Chern. Oxygen Demand, ng/1 ,,
--;,1~.} ll li JJl ll. l2.(D) ll
Time: 11:06 10:29 18:23 18:15 15:58 16:45
~~ Air Tenp, oc 14 14 16 16 17 17
Precipitation, inches 0 0 0 0 0 0
.,...,..,.<! Cloud Cover, % 50 50 75 75 100 100
r,r· Dissolved Oxygen, mg/1 9.9 10.7 10.8 9.9 10.4 10.5 ~: Tanperature, °C 12 11 12 12 11 12
pH, Iii Units
[ Settleable SOlids, ml/1 <..O.l ~0 .. 1 32 8.5 2.0 0.2
Flow, cfs 1.5(E) 3.0 (E) 7.5 (E) lO(E) 8.,3 8.2
'1\lrbidi ty, NI'U 1400 6700 2800 3600 3200
T. suspended Solids, ng/1 1990 1450 13000 5170 2980 1770
~' Olem. Oxygen Derand, mcVl
Ccmnents:
r,, 1. Cubic yards moved/day: Warner: 0; Haskins: 450-550. . ' 2 .. Fquipnent used, hours/day: Haskins: Drag1ine, 988/6 hrs • ~ 3. Problems:
4. other Comments: Trammel will operate at its present location for at least 2 weeks
~··· therefore giving us our 50 sample days. Low water conditions have limited sluicing k to 6-7 hours/day.
[' .
• .;>
~: \
I·
~'
Cooments:
1. l"'!ubic yards moved/day: Warner: 0; Haskins: 375-470.
2~ ~ipnent used, hours/day: Haskins: Dragline, 988/5 hrs; D-8 stripping for both
Haskins and Wa.tner.
3. Problans:
4. Ot.'l~r Caments: J. Wel.lrnan arrived from Fairbank-s. Decided to have ta1lings pushed
into th~ pond influent area in cul effort to incr~ase settling pond efficiency.
--··
~ugust 9 , 19 81
Time:
Air Tanp, °C
Precipitation, inches
Cloud Cover, %
Dissolved Oxygen, m:Vl
Temperature, °C
fi:l , Iii Units
Settle~1e Solids, ml/1
Flow, cfs
Turbidl ty, Nltf ·
T. Suspended Solids, ng/1
Olem. Oxygen Demand, mg/1
Time:
Air Temp, °C
Precipitation, inches
Cloud Cover, %
Dissolved Oxygen, mg/1
Temperature, °C
pH, pH Units
Settl#\;~·-?le Solids, m.l/1
Flow, cfs
Turbidity, Nru
T. Suspended SOlids, mg/1
Chern. Oxygen Demand, ng/1
Time:
A..i.r Temp, °C
Precipitation, inches
Cloucl Cover, %
Dissolved Oxygen, mg/1
Tenperature, oc
f:B, pH Units
Settleable Solids, ml/1
Flow, cfs
Turbidity, :mu
T. Suspended Solids, nq/1
~ ::n::en Demnd, nq/1
DEC DEMJNSTRATION PROJECT
FIEW mTA
l
09:30
12
0
75
10.8
9
( 0.1
3.4
4.6
35.5
1
WJ
sample
Not
Taken
ll
12:31
14
0
100
10.8
12
<0.1
1.5
750
520
2.
10:27
12
0
60
10.0
12
(0.1
0.8{E}
24.0
62.0
.a
~
sample
Not
Taken
14.
13:16
13
0
100
10.8
11
0 .. 6
0.2 (E)
600
19700
SAMPLE I.QCATION
l .4.
09:03 10:10
12 12
0 0
75 60
10.7
8
.(0.1
3.5 (E)
1.6
4.6
.2.
1:..:.:21
13
0
100
11.3
11 .
(0.1
150 ao.o
JJl
Tr~l
Not
Operating
11 .. 8
11
29
12(E)
6600
11700
lO.
13:26
14
0
100
11.2
11
130
7 .. 5(E)
15000
40000
ll.
15:28
16
0
50
10.6
11
0.8
2.2(E)
1000
540
1. Cubic yards rooved/day: Warner: 500-625~ Haskins: 300-375.
Day 37
5..
09:36
12
0
75
11.8
9
~ 0.1
l.O{E)
1.6
8 .. 1
.ll,
13:35
14
0
100
10.6
11
22
10(E)
6600
8570
ll(C)
15:10
16
0
50
11.7
12
0.1
2.8
1000
880
12:17
14
0
100
10.2
12
< 0.1
<O.l(E)
BOO
370
l2.(D)
12:22
14
0
100
10.4
11
<. 0.1
1.6
2300
720
ll
15:18
16
0
50
10.9
12
0.2
2.7
900
530
f, ·2. Equi~nt usedv hours/~li\Y: Warner: D-8 chasing tailings, pushing pa.}-rlirt. 988 loader/
~ 5 hrs ..
3 • Problems:
4. Other Caments: warner sluicing for the first time i.a"l 2 weeks~ using new sluice box.
11
rj
'
i
r
~
~·-
f
r
'f ~l
l
l
August 12, 1981
Time:
Air Temp, °C
Precipitation, inches
Cloud <.:over, %
Dissolved Oxygen, mg/ 1
Temperature, °C
pi, pH Units
Settleable Solids, ml/1
Flow, cfs
Turbidity, m:u
T. Suspended Solids, ng/1
Chern. Oxygen De!Pand, rng/1
Time:
Air Temp, °C
Precipitation, inches
Cloud Cover, %
Dissolved Oxygen, mg/1
Temperature, °C
pH, J:i1 Units
Settleable Solids, tnl/1
Flow, cfs
'!Urbidi ty, NIU
T. susp:ilded SOlids, rng/1
Clem. Oxygen Demand, rrg,/1
Time:
Air Temp, °C
Precipitation, inches
Cloud Cover, %
Disso1 ved Oxygen, m:J/1
Temperature, °C
Fi!f pH Units
Settleable Solids, ml/1
FlCM, cfs
Turbidity, N'ID
T. Suspended Solids, ug/1
Clem. Oxygen Demand, mg/1
Comme:nts:
DEC DEM:>NSTRATION PRQJECr
FIELD :Dtt\TA
l
21:17
10
0
100
10.3
7
6.7
<0.1
2.0(E)
450
490
2
WJ
Sample
Not
Taken
ll
16:18
20
0
100
10.1
13
6.4
0.10
6.0
1200
1070
2.
Dry
.B.
WJ
Sample
Not
Taken
.a
Dry
SAMPLE WCATION
.l A.
WJ
Sample
Not
Taken
.2.
16:00
20
0
100
10.7
13
6.5
0.2
360
355
lQ.
16:42
20
0
100
11.1
14
5.9
110
7 .. 5 (E)
2500
2770
l'k>t
Sluicing
l.Q.
15:51
20
0
100
11.0
14
5.9
15.0
7 .5 (E)
10~00
880
ll
16:10
20
0
100
10.6
12
6.3
1.0
9.0 (E)
2000
1740
Day 38
5.
WJ
Sample
Not
Taken
ll
15:38
20
0
100
10.7
13
6.0
1 .. 0
9.0 (E)
1500
1220
l2.(D)
21:45
10
0
100
11.8
10
6.5
<.0.1
0.9
1500
1070
.2.
21:37
10
0
100
11.2
10
6 .. 0
<.0.1
<.0.1
1400
1220
ll(B)
16:29
20
0
100
10.7
13
6.2
0.1
6.2
1400
1360
ll
21:54
10
0
100
12.3
9
c ") u .... G.
0.1
0.9
1500
880
1. Cubic yards moved/day: Warner: 400-500; Haskins: 675-850.
2. Equipnent used, hours/day: Warner: D-9 pusr.d.ng tailings, 988 loading slick plate/
4 hrs; Haskins: Dragline, D-8 pushing,paydirt and tailings/9 hrs.
3 • Problems:
4. other Ccrnroonts: The settling pond modifications is in place. A berm of tailings
approximately 3' high, 72' long, and 31' wide was put in at the influent end of the
settling pond creating a small pond approximately 100 1 above t~e settling pond.
August 13, 1981
'rime:
Air Temp, °C
Precipitation, inches
Cloud Cover, %
Dissolved Oxygen, ~/1
Temperature, °C
tfl, Ffl Units
Settleable Solids, ml/1
F].ow, cfs
'1\J.rbidity, NTU
T. Suspended Solids, mg/1
Olem. Oxygen Demand, mg/1
Time:
Air Temp: °C
Precipitation, inches
Cloud Cover, %
Dissolved Oxygen,, rng/1
Temperature, °C
pH, pH Units
Settleable Solids, mall
Flow, cfs
Turbidity, NIU
T. SUS:FEnded Solids, mg/1
C1em. Oxygen Demand, rng/1
Time:
Air Temp, oc
Precipitation, inches
Cloud-Cover 1 %
Dissolved Oxygen, mg/1
Temperature, °C
pH, pH Units
Settleable Solids, ml/1
Flow, cfs
Turbid~ty, NTU
T .. Suspended Solids, mg/1
Chern. Oxygen Danand, mg/1
Comments:
DEC DEMJNSTRATION J::::xnECT
.1-"IEID MTA
SAMPLE .I.QCATION
.l
13:24
13
0
100
10.7
8
6~8
1 .. 2
2 .. 1
700
650
2
WJ
Sample
Not
Taken
ll
11:03
12
0.01
100
12.1
9
6.2
"0.1
3.5
1400
720
2. l ~
Dry
.a
~
sample
Not
Taken
li
Dry
12:52
13
0
100
11.0
7
6.4
<.0.1
2.0 {E)
24
42.4
2.
14:16
13
0
100
11.8
10
7.0
< 0.1
360
515
lO.
14:38
13
0
75
12.0
10
6.4
75
7.4
7700
31400
19:05
11
0
50
12.0
8
6.9
27
12(E)
6200
5210
l.Q.
10:37
12
0.01
100
" 12.8
9
5.9
26
7 .5 (E)
5000
9900
ll.
15~39
14
0
75
10.8
10
6.6
1.8
8.2
2300
2010
1.. Cubic yards moved/day: Warner: 400-5007 Haskins: 525-650.
Day 39
5.
13:15
14
0
100
11.6
9
7.0
<.0 .1
0.2(E)
3.0
1.2
ll.
10:46
12
0.01
100
12.1
10
6.1
0.1
1.0(E)
1400
1750
ll(B)
16:19
15
0
60
11.3
12
6.6
<.O.l
6.8
1200
660
.2.
16:12
14
0
60
10.3
11
6.5
0.2
0.1
1200
770
ll(C)
10:55
12
0 .. 01
100
12.3
10
6.5
,0.1
3.8
1100
970
ll
16:25
15
0
60
10.7
11
6.7
<.0.,1
6.6
900
990
2. Equipnent used, hours/day: Warner: D-9, 988/4 hrs~ Haskins: Dragline, D-8/7 hts.
3. Problems: Haskins 988 loader broken down.
4. Other Corrrnents: Warner laid off 4 people today due to low water condi.tions ..
~-
'•
"
,,
;l ,. "; DEC DEM:>NSTRATION PRQJECr
FIEI:D MTA
~1 August 14, 1981 Day 40
d ~~ ' SAMPLE IOC.\TION
l 2. J. .4. .5. .6.
p
Time: 12:21 D:cy WJ 18:15 WJ 13:04
Air Temp, °C is Sample 13 Sample 18
Precipitation, inches 0 Not 0 .. 02 Not 0
~ Cloud Cover, % 75 Taken 100 Taken 75" ~
i
Dissolved Oxygen, mg/1 11.0 12.2 10.7
~"' Temperature, oc 8 8 11
~ !i1, pH Units 6.6 6.8 6.5
l= Settleable Solids, rnl/1 2.5 32 0.3
Flow, cfs 3.8 12(E) <0.1
·-· Turbidity, Nr"J 1200 6400 1800 .'f!'
"-T. Suspended Solids, ng/1 2070 9090 1250
Clem. Oxygen Demand, mg/1
rr 2 .a .9. lO. ll l2.(B)
.i TL11e: ~ w:l 13:30 13:37 14:15 12:47 i.
{ Air ~remp, oc Sample S'.:tmp1e 17 17 17 18
Precipitation, inches Not Not 0 0 0 0
"~ Cloud Cover, % Taken Taken 75 75 75 75
...
Dissolved Oxygen, mg/1 11.0 11.6 10.0 10.9
Temperature, oc 10 10 10 10
1 pH, FH Units 7.0 6.5 6.6 6 .. 4
Settleable Solids, ml/1 <0.1 75 2.0 0.5
Flow, cfs 7.8 7.7 3.7
f-t Turbidity, ~--ro 500 7900 1800 1600
r·
' T. Suspended Solids, mg/1 270 29900 2130 1370
~ 1 Chern. Oxygen Demand, ng/1
ll ll .l.Q. ll. ll(C) ll
:( Time: 12:56 Dry 16:15 16:26 16:34 16:40
!~ Air Tanp, °C 18 14 14 14 12
Precipitation, inches 0 0.02 0.02 0.02 0.02
~f > Cloud Cover, % 7§ 100 100 100 100
Dissolved Oxygen, mg/1 10.9 11.4 11.2 11.3 11.3
'I'E!mperature, °C 10 10 10 10 ' 10
fil, pH Units 6.6 6.8 6 .. 6 6.5 6.6
,'l Settleable Solids, ml/1 <O.l 14.0 3.7 0.4 0.3 ·-· Flow, cfs 3.5 7.5 (E) 7 .. B(E) 6.5 6.2
Turbidity, Nn.l 1000 2300 2600 1600 1000
T. Suspended Solids, ng/1 950 3690 2450 1340 1230
~·I Clem. OXygen Demand" mg/1
Cooments:
,. 1. Cubic yards mcveq(day: Warner: 200-250; Haskins: 415-515. ·-,., Equipnent used, hours/day: Warner: D-9, 988/2 hrs sluicing; Haskins: Dragline, D-8/ -'•
5.5 hrs ..
3. Problems: Constant problens with the flow meter.
~;. 4. Other Conments: '!be rnoc:lification to the settling pond appears to be reducing the
settleable solids entering and exiting the pond. Warner will not be going down to
claim 5 below ~~s season.
•
August 15, 1981
Time:
F; Air Tanp, °C
Precipitation, inches
Cloud Cover, %
-
!
··,
[
Dissolv~ Oxygen, mg/1
Temperatt.. ... e, °C
pH, pH Units
Settleable Solids, ITU/1
FlC'ft\1, cfs
Turbid! ty, NIU
T. Suspended Solids, rrg,/1
Clem. Oxygen Demand, mg/1
Time:
Air Temp, °C
Precipitation, inches
Cloud Cover, %
Disso1 ved Oxygen., mg/ 1
Temperature, °C
pH, Iii Units
Settleable Solids, ml/1
Flow, cfs
Turbidity, NIU
T. Suspended Solids, mg/1
Chem. ~gen Demand, mg/1
Time:
Air Tenp, °C
Precipitation, inches
Cloud Cover, %
Dissolved Oxygen, mg/1
Tanperature, °C
r;H, pH Units
Settleable Solids, ml/1
Flow, cfs
Turbidity, NrU
T. Suspended Solids, rrg/1
Clan. Oxygen ]Jgnand, ng,/1
Corcments:
DEC I>EX.'fiSTRATION PRC\JECT
FIEID Df\TA
l
15:50
13
0.58
100
12.2
8
6.6
0(18
2.1
1600
1600
2
rJJ
Sanple
Not
Taken
ll
10:49
12
0
50
11o6
10
6.6
0.2
3.5
1000
840
Dry
.a
NJ
Sanple
Not
Taken
.a
Dry
WJ
Sample
Not
Taken
.i
14:51
13
0
100
10.9
11
6.7
2.8
1200
2780
JJl
15:36
13
0.58
100
11.9
10
6.5
50
7.5 {E)
8400
20900
13:25
14
0
75
12.3
8
7.0
40
12
7000
22200
lO.
14:,-!1
14
0
100
11.7
10
6.7
35
7.5 (E)
2900
11700
.ll
15:02
14
0.58
100
11.4
10
6 .. 6
3.0
8.0 {E)
1600
2880
1. Cubic yards moved/day: Warner.: -400-500; Haskins: 640-800.
Day 41
5.
WJ
Sample
Not
Taken
ll
10:25
12
0
50
11.9
8
6.5
2.3
3.8(E)
1500
1910
ll{C)
15:11
14
0.58
100
12.1
10
6.6
0.2
5.6
1200
1330
.2.
10:40
12
0
50
11.0
10
6.6
0.6
<..0 .. 1
1200
1140
ll{B)
10:36
12
0
50
11.6
9
6.5
1.0
3.7
1400
1280
ll
15:23
13
0.58
100
11.7
10
6.6
0.2
5.6
1200
990
2. Equipnent used, hours/day: Warner: D-9, 988/ 4 hrs7 Haskins: Dragline, D-8/8.5 hrs.
3. Problans: Haskins 988 loader sti:;.l broken dawn. Warner D-8 going back to NC cat.
4. Other canments:
.
f >
l'
''
DEC DEK>NS!i<ATION PRQJECr
FIEID DATA
August 16, 1981 Day 42
SAMPLE LOCATION
~ 2. J. .4. 5. 2.
Time: l0:30 Dry WJ 9:30 WJ \~
Air Temp, °C 9 Sample 10 Sample Sample
Precipitation, inches 0 Not 0 Not Not
Cloud Cover, % 75 Taken 75 Taken Taken
Dissolved Oxygen, mg/1. 12.1 12 .. 2
Temperature, °C 6 8
r:H, pH Units 6.7 6.4
Settleable Solids, ml/1 1.3 21
Flow, cfs g·.o 12
Turbidity, N'IU 600 1700
T. Suspended Solids, ma_/1 615 8230
Chen. OXygen Demand, ~1
2 .8. i lll ll ll(C)
Time: WJ tiQ 10:06 16:11 16~50 15:00
Air Temp, °C Sample sample 10 12 ll 12
Precipitation, inches Not Not 0 0 0 0
Cloud Cover, % s-l'aken Taken 75 75 75 75
Dissolved Oxygen, ng/1 11.1 11.7 10.8 11.3
Temperature, °C 8 8 9 10
pH, pH Units 6.6 5.7 6.4 6.7
Settleable Solida, ml/1 ~0.1 ]~15 3.0 <.0.1
Plow, cfs 7.6 8.5(E) 1.4
Turbidity, Nru 550 9600 1500 950
T. Suspended Solids, mg/1 740 26900 2900 1050
Clem. Oxygen Demand, ng/1
ll l! lQ. ll l2.(B) ll
Time: 14:45 10:11 Trorrmel 18:24 18:30 18:38
Air Tanp, °C 12 10 Not 11 11 10
Precipitation, inches 0 0 Operat~ng 0 0 0
Cloud Cover, % 75 75 50 50 50
Dissolved Oxygen, mg/1 10.4 11.8 10.9 11.1 10.7
Temperature, °C 10 7 9 10 10
Pf, pH Units 6.8 6.7 6.3 6.6 6.6
Settleable Solids, ml/1 LO.l 9.0 1.5 0.1 4 0.1
Flow, cfs 1.4 lO(E) 5.0 (E) 4.6 4.4
Turbidity, NlU 1200 2400 1300 1100 1100
T. Suspended Solids, nw'l 720 4150 1600 1260 1160
Clem. Oxygen Demand, mg/1
O:>nrnents:
1. CUbic yards moved/day: Warner: 700-875; Haskins: 150-200.
2. Equipoont used, hours/day: Warner: D-9, 988/7 hrs: Haskins: Drag1ine, 988/2 hrs ..
3. Problems: Tratrnel needed welding. Haskins D-8 needs new tracks.
4. Other Gomments: Warner gets a full shift sluicing. Creek water level dropping rapidly.
r i.
';
~
fJ )'
I
~,,
p
I,
~?
~ .
L
August 17, 1981
Time:
Air Tanp, oc
Precipitation, inches
Cloud Cover, %
Dissolved Oxygen, ng,/1
rrcemperature, oc
J:fi, pH Units
Settleable Solids, ml/1
FlO\v, cfs
TUrbidity, NID
T. SusJ;ended Solids, mg/1
Chern. Oxygen Demand, rng/1
Time:
Air Temp, oc
Precipitation, inches
Cloud Cover, %
Dissolved Oxygen, rng/1
TemJ;erature, °C
pH, fii Units
Settleable Solids, ml/1
Flow, cfs
Turbidity, NlU
T. suspended SOlids, mg/1
Chan. Oxygen Demand, ng/1
Time:
Air Temp, °C
Precipitation, inches
Cloud Cover, %
Dissolved Oxygen, mg/1
Temperature, °C
pH, pH Units
Settleable Solids, m1/ 1
Flow, cfs
'li.lrbidity, NIU
To Suspended Sol.lds, m3/l
Clem. Oxygen Demci.nd, mg/1
Cormnents:
DEC DFX.>NSTRATION PRQJEcr
FIEID DA.TA
l
14:05
20
0
20
11.6
8
6.9
1.9
7.8
,550
1010
2
WJ
Sample
Not
Taken
ll
14:34
20
0
50
10.4
9
6.7
<0.1
1.2
900
870
2.
Dry
.a
~~
Sample
Not
Taken
.a
10:05
15
0
20
11.6
7
6.7
8.0
7.0 {E)
900
2720
SAMPLE IDCA~lQB
.l
13:15
20
0
20
11.7
6
6 .. 9
< 0.1
6.5 (E)
5 .. 6
1 .. 1
.9.
10:12
15
0
20
10.8
7
6.6
<0.1
700
380
lQ.
17:55
18
0
10
11.7
8
6.4
78
7.5 (E)
11800
35600
!.
10:44
15
0
20
11.8
6
6.5
26
12(E).
3900
8960
lQ.
14:51
20
0
50
12
8
6.7
125
7.6
13100
49200
ll
18:03
18
0
10
10 .. 8
9
6.5
7.0
8.5 {E)
3400
5270
1. Cubic yards rnovedVday: Warner: 850-1075; Haskins: 250-325.
Day 43
5.
13:55
20
0
20
11.7
18
7.0
~0.1
1.5 (E)
6.0
6.2
ll
15:44
20
0
50
10.6
10
6.7
5.0
8.5 (E)
1800
4270
l.2,(C)
18:12
17
0
10
11.2
10
6 .. 5
0.4
6.5
1400
1620
.6.
~
Sample
Not
Taken
l2.(B)
14:20
20
0
20
11 .. 5
8
6.8
<0.1
1.2
900
840
ll
18:19
18
0
10
10 .. 7
10
6.8
0.4
6.2
1200
1630
2. Equipnent used, hours/day: Warner: D-9, 988/8.5 nrs; Haskins: Dragline, 988/3.5 hrs.
3. Problems: Drive line broke on the tronmel.
4. Ot.'1.er Comments:
August 18, 1981
Time:
Ait Tenp, °C
Precipitation, inches
Cloud Cover, %
Dissolved Oxygen, mg/1
Temperature, °C
pH, pH Units
Settleable Solids, ml/1
Flow, c.fs
Turbidi.ty, NW
T~ Suspended Solids, rrg/1
Chern. Oxygen Demand, mg,/1
Time;
Air Temp, °C
Precipitation, inches
Cloud Cover, %
Dissolved Oxygen, mg/1
Temperature, °C
I=fi, pi Units
Settleable Solids, ml/1
Flow, cfs
Turbidity, NlU
T .. Suspended Solids, mg/1
Chern. Oxygen Demand, ng/1
Time:
Air Tenp, oc
Precipitation, inches
Cloud Cover, %
Dissol voo Oxygen, mg/1
Temperature, °C
pH, pH Units
Settleable Solids, ml/1
Flow, cfs
Turbidity, NTU
T. Suspended Solids, m:v'l
Clem. Oxygen DEmand, m;/1
Comments:
DEC DEM:>Nsr.mATION PROJECT
FIEID DA.TA
~
12:11
20
0
40
12.8
7
6.8
1.1
lO(E)
150
472
]_
WJ
sample
Not
Taken
ll.
14:15
21
0
50
11.0
8
6.5
0.4
6.6
3000
1890
2.
Dry
.a
WJ
Sample
Not
Taken
l!
12:55
21
0
50
10.4
10
7.0
10
0.5 (E}
1500
1960
SAMPLE lOCATION
J. .4.
WJ
Sample
Not
Taken
i
12:48
21
0
50
10.9
8
6.7
<0.1
1600
990
l.Q.
16:09
20
0
60
11.7
8
6.4
72
7.5 (E)
8600
30000
12:22
20
0
40
12.5
7
6.2
32
12(E)
3500
11000
l.Q.
12:39
21
0
50
12.2
7
6.3
37
7.0
7700
13600
ll
16:17
20
0
60
10.8
9
6.6
9 ... 5
8.0(E)
2800
6210
1. Cubic yards moveq(day: Warner: 800-1000; Haskins: 750-940.
Day 44
5.
WJ
Sample
~t
Taken
ll
13:31
22
0
50
11.0
9
6.6
5 .. 5
7.9
3200
4400
ll(C)
16:36
20
0
60
11.6
10
6.6
0.7
6.5
2900
2540
~
w:2
Sample
Not
Taken
l2.(B)
14:25
21
0
50
11.4
9
6.6
0.2
6.5
1900
1720
ll
16:27
20
0
60
10.7
10
6.6
0.7
6.6
2900
2320
2. Fquipnent used, hours/day: Warner: D-9, 988/8 hrs; Haskins: Dragline, 988/10 hrs.
3. Problems:
4. Other Comments: Both operations ran smoothly with no problems.
August 19, 1981
Time:
~/ Air TsnPr oc
Precipitation, inches·
cloud cover, %
·r oissol ved Oxygen, mg/1
ianoerature, oc
fH,~pH Units
'? Settleable Solids, ml/1
Flow, cfs
-Turbidity, NTU
T. suspended Solids, rng/1
Chan. Oxygen Demand, mg/1
Time:
"? Air Temp, oc
·, Precipitation, inches
Cloud Coverr %
·;. Dissolved Oxygen, mg/1
Temperature, °C
pH, pH Units
~ett1eable Solids, ml/1
_low, cfs
·~· Turbidity, NIU
T. SUSf:Ended Solids, mg/1
·· Chan. Oxygen Demand, ng/1
Time:
. Air Tenp, °C
Precipitation, inches
.J Cloud Cover, %
·; Dissolved Oxygen., rng/1
Temperature, °C
~'. pH, pH lJni ts
Settlee.ble Solids, ml/1
Flow, cfs
., Turbidity, NTU
T. Suspended Solids, mg/1
· Olem. Oxygen Demand, mg/1
·· Comnents:
DEC DEMlNSTRATION PROJECT
FIEID MTA
l
10:05
13
0
75
12.3
6
2.0
7.8
700
1400
]_
WJ
Sample
Not
Taken
ll
14:27
14
0
100
11.4
9
0.6
6.3
1600
1980
2.
Dry
.a
WJ
Sclnple
Not
Taken
l4.
12:55
14
0
75
11 .. 3
9
17
1.1
1900
4950
SAMPLE I.DCATION
J. .4.
WJ
Sample
Not
Taken
~
13:00
14
0
75
11.1
9
<0.1
550
196
lQ.
16:20
14
0.2
100
12.2
8
42
7.8
9600
6200
09:54
13
0
75
12.3
6
29
12(E)
2600
4500
lQ.
13:05
14
0
75
12.1
9
100
7.8
11200
19500
ll
16:26
14
0.2
100
11.6
8
5.0
8.0 (E)
3100
2710
1. Cubic yards moved/day: Warner: 700-875; Haskins: 525-650.
Day 45
5..
WJ
Sample
Not
Taken
ll
13:45
15
0
75
11.5
9
8.0
8 .. 0
6600
4540
ll(C)
16:41
13
0 .. 2
100
12.3
9
0116
6oS
1800
470
~
14:35
14
0
100
10 .. 8
10
2.8
< 0.1
2900
2980
l2.(B)
14:40
14
0
100
11.6
9
0.4
6.5
1900
1210
ll
16:34
13
0.2
100
11.8
9
0.6
6.3
1800
910
2. Equipnent used, hours/day: Warner: D-9, 988/7 hrs; Haskins: drag1ine, 988/7 hrs.
:_~ 3. Problem~; pH meter will not calibrate or stabilize its read-outs.
'' ..1
4. Other,· Conments: Warner partial clean-up in the afternoon. Haskins D-8 rwming-first
time they· have had tractor running in a week. (3 others down).
August 20, 1981
Time:
Air Temp, °C
Precipitation, inches
Cloud Cover, %
Dissolved Oxygen, mg/1
Temperature, °C
pH, pH Units
Settleable Solids, rnl/1
Flow, cfs
Turbidity, NTU
T. Suspended Solids, mg/1
Chern. Oxygen Demand, mg/1
Time:
Air Temp, °C
Precipitation, inches
Cloud Cover, %
Dissolved Oxygen, mg/1
Temperature, °C
pH, I;B Units
Settleable Solids, ml/1
Flow, cfs
'1\lrbidi ty, NlU
T .. Suspended Solids, mg/1
Chen. Oxygen Demand, tn3/l
Time:
Air Temp, °C
Precipitation, inches
Cloud Cover, %
Dissolved Oxygen, mg/1
TE!nperature, °C
pH, pH Units
Settleable Solids, m1/ 1
Flow, ·cfs
Turbidity, NTU
T. Suspended Solids, ng/1
<llem. Oxygen Demand, mg/1
Ccmnents:
DEC D~TION PROJEcr
FIEID rATA
Day 46
SAMPLE IDeATION
l
13:07
7 o.os
100
13.2
6
6.6
1.4
12(E)
1800
1060
2
V{J
Sample
Not
Taken
ll
10:47
7
0.01
100
12.1
8
6.4
0.4
5,7
2000
1600
Dry
.a
WJ
Sample
Not
Taken
l!
13:54
7
0.08
100
13.2
7
6.8
2.0
7.9
500
465
J. .4.
WJ
Sample
Not
Taken
i
13:49
7
0.08
100
13.5
8
6.7
<0.1
3'i0
80.0
.10.
13:43
7
0.08
100
13.2
7
6.4
30
6.7
2500
6700
Not WJ
Sluicing Sample
lQ.
10:34
7
0.01
100
12.7
7
5.9
79
7.5 (E)
7400
28300
ll
14:56
6
0.08
100
12.5
8
6.4
6.0
7.8
3400
4780
Not
Taken
ll
10:40
7
0.01
100
12.0
8
6.3
7.0
8.0 (E)
3200
4060
ll(C)
15:51
6
0.08
100
13.0
8
6.4 o.8
6.5
2200
2530
1. Cubic yards moved/day: Warner: 0; Haskins: 700-900 ..
2. Equipnent used, hours/day: Warner: 0; Haskins: Dragline, 988/9.5 hrs.
3 • Problems:
15:56
6
0.08
100
11.9
9
6.4
2.9
<'0 .. 1
1000
2150
J.2.(B)
10:57
7
0.01
100
12.5
8
6.4
0.4
5 .. 8
1600
1160
ll
15:44
6
0.08
100
12.5
8
6.6
0.7
6.4
2300
2050
4. Other Corrments: Warner clean-up and corrmencement of moving sluice oox, pipes, and
slick plate up the creek 300'.
..-· F .,
-
r DEC DE'M)NSTRATION PRQJECr
'· FIEID DATA
'·· t 21, 1981 Day 47
Aug us SAMPLE I.QCATION
;·~ ~ 2. ~ !. .5. .2.
12:26 Dry 10:06 Not 12:37 13:50
.. TiJne: oc 11 9 Sluicing 11 11
r· Al! TE!OP' . inches 0.1 0.02 0.1 0.01 precipitatlon, 100 100 100 lOO cloud cover, %
Dissolved Oxy~en, rrg/1 12.9 13.1 13.0 12.1
Temperatu:e, C 6 4 5 8
6.6 6.6 6.8 6.2 I, fiJ UnltS . ~ttleable SOllds, ml/1 6.0 ~0 .. 1 <.0 .1 7.0
26(E) 18(E) 4.5 {E) < 0.], Flo,.;, cfs
TUrbidity, NIU . 800 7.2 14 2800
T suspended Sollds, mg/1 1400 1.4 27.6 4600 ciem. oxygen oemand, mg/1
2 .a .9. JJl. ll ll(B)
Time: WJ w;J 13:07 10:36 10:45 11:02
AJ.r Tanp, oc Sample Sample 11 10 11 11
''i Precipitation, inches Not Not 0.1 0.02 0.02 0.02
cloud cover, % Taken Taken 100 100 100 100
J
Dissolved Oxygen, mg/1 12.0 13.3 12.1 12.5
Temperature, oc 6 7 8 8
FiJ, r:£ Units . , 6.5 5.7 6.4 6.5
Settleable Sol1oa! ml/1 0.~2 95 7.0 0.5
Flow, cfs 7.5 (E) 8.0 (E) 8.7
Turbidity, NIU 450 9900 3800 1800
T. SUSt:€nded Solids, rng/1 1410 37600 9110 1290
-~ 01an. Oxygen Demand, mg/1
ll li lO. ll ll(C) ll
Time: 10:52 13:13 13:00 13:35 13:45 13:55
Air Temp, °C 11 11 11 11 11 11 ,, !'n:~cipitation, inches 0 .. 02 0.1 0.1 0.1 0 " 0.1 ! a A ..
'
_) Cloud Cover, % 100 100 100 100 100 100
··~ Dissolved Oxygen, mg/1 12.1 12.8 13.0 13.1 13.1 12.6
Temperature, °C 8 6 7 8 8 8
,.;t [:li, pH Units 6.5 6.4 5.4 6.2 6.2 6.4
Settleable Solids, ml/1 0.5 9.0 45 9.0 0.7 0.6
~ Flaw, cfs 8.6 30(E) 7.5 (E) f3.0(E) 1l(E) 11(E)
Turbidity, NIU 2300 1400 7800 3400 1600 1500 _j T. sus~nded Solids, ID3/1 1390 2510 12200 4700 2080 1890
') Cllem~ Oxygen Danand, 11¥311
,_r Cormlents:
l. Cubic yards moved! day: Warner: 0; Haskins: 600-7 50.
2. ~uipnent used, hours/day: Warner: D-9, 988 to move pipes, etc./9 hrs; Haskins:
i Dragllne, 988/8 hrs.
·~· 3 • Problems:
4. Other Caranents: Warner moving sluicing operation upstream.
' .:1'
1>
r\
L
r··
I
\ DEC D~TION PRQJECI'
r· FIEW Dt\TA
!'' August 22, 19 81 Day 48 i 1 SAMPLE IDC'ATION
~ 2. J. !. .5. .[
""' r Time: 12:25 Dey WJ Not ~ W,J r ! Air Tenp, oc 12 Sample Sluicing Sample Sample
Precipitation, inches 0 Not Not Not .....
Cloud Cover, % 85 Taken Taken ic Taken
~' \
!
Dissolved Oxygen, mg/1 12.6
p Temperature, oc 6
' pi, fil Units 6.5 I, Settleable SOlids, ml/ 1 1.0
FlOW', cfs 58 rl TUrbidity, NIU 85
T. Suspended Solids, m;/1 136
Chern. OXygen Demand, mg}l
r: 1 .a. .9. l.O.. ll. l2.(B)
Time: WJ WJ 10:41 09:53 10:04 10:27
[' Air Tenp, oc Sample Sample 8 8 8 8
Precipitation, inches Not Not 0 0 0 0
f,
f
Cloud Cover, % Taken Taken 75 100 100 90
' Dissolved Oxygenr mg/1 12.1 12,5 12.0 12.5
r. Temperature, oc 6 6 6 7
I J:ii, Iii Dni ts 6.3 5.8 5.9 6.3
Settleable Solids, ml/1 0.2 77 10.5 0.6
Flow, cfs 7.5 (E) 8.0 (E) 7.5
r· Turbidity, NJlJ 500 11800 3500 1500 ' i T. Suspended Solids, mg/ 1 "''35 59800 2400 990 I ~ :3
Chan. Oxygen Demand, rrg,/1
f') ll li lQ. ll ll(C) u
Time: 10:17 10:46 14:11 14:26 14:43 14:31 r· Air Temp, oc 8 8 12 12 12 12
Precipitation, inches 0 0 0 0 0 0
r, Cloud Cover, % 100 75 75 75 75 75 ,,
l Dissolved Oxygen, m:;Vl 12.3 13.4 12.5 12 .. 0 12.4 11.9
Temperature, °C 7 6 6 7 8 8 ! : J:ii, til Units 6.2 6.4 6.9 6.2 6.3 6 .. 3 ! ~ttleable SOlids, ml/1 0.3 2.5 2·~ 7.5 1.0 0"9 •.. ,_}
Fl~~,. cfs 7.5 60(E) 7.5 (E) B.G{E) 7.5 7.5
I., Turbidity, Nro 1900 500 1600 2500 2100 1800
k T. Suspended Solids, rrg/1 800 190 5020 3440 1740 1920
.. _l Olen. Oxygen Demand, mg/1
Carrnents:
1. Cul'ic yards moved/day: Warner: 0; Haskins: 675-850.
2. &;!uipnent used, hours/day: Warner: 0; Haskins: D-8 stripping, Dragline, 988/9 hrs. ~
! r· 3. Problems: One of the cups on the flCM meter broke off; glued it on. ' I 4ti Other Oaroments: Haskins operation running smoothly. Warner moving sluicing 9peration f·, l upstream.
~ ~
~: . .;
r:
p
I ' [ .
!,
~
August 23, 1981
Time:
Air Temp, oc
Precipitation, inches
Cloud Cover, %
Dissolved Oxygen, mg/1
Temperature, oc
pH, pH Units
Settleable Solids, rnl/1
Flow, cfs
Turbidity, NIU
T .. Suspended Solids, ng/1
Chan. Oxygen Demand, mg/1
~rime:
Air Temp, oc
Pr-ecipitation, inches
Cloud Cover, %
Dissolved Oxygen, mg/1
Temperature, °C
pH, pH Units
Settleable Solids, ml/1
Flow, cfs
Turbidity, NIU
T. Sus~nded SOlids, mg,/1
Olem. Qxljgen Demand, mg/1
Time:
Air Tenp, °C
Precipitation, inches
Cloud Cover, %
Dissolved Oxygen, mg/1
Temperature, °C
pH, pH Units
Settleable SOlids, ml/1
Flow, cfs
Turbidity, NIU
T. Suspended Solids, mg/1
Olem. Oxygen Darland, mg/l
C.ontm6nts:
DEC DEMJNSTRATION PRQJECT
FIELD MTA
l
13:20
19
0
10
12.3
6
6.5
<0.1
45
170
325
2
WJ
sample
Not
Taken
ll
15:24
20
0
10
11.9
9
6.6
<.O.l
1.7
750
295
Dry
.8.
~
Sample
Not
Taken
.l.4.
13:45
20
0
10
12.5
8
6.3
3.2
4.8(E)
500
290
,SAMfi£ I.DC'ATION
1 J.
WJ
Sample
Not
Taken
.2.
13:52
20
0
10
11.7
7
6.3
<.0.1 ...
200
285
lO.
Tronm=l
Not
O};erating
Not
Sluicing
lQ.
Tranmel
Not
Operating
ll
19:15
l5
0
5
11 .. 8
8
6.3
(0.1
1.5(E)
60
72
1. Cubic yards moved/day: Warner: 0; Haskins: 0.
Day 49
5.
Wj
Sample
Not
Taken
ll.
15:40
21
0
10
11.2
10
6.3
<.O.l
1.5
100
105
ll{B)
19:10
15
0
5
12.2
9
6.3
"0.1
1.8
700
265
2. Equipnent used, hours/day: Warner: stripping new mine cut with D-9/9 hrs.
3. Problems: Flow m;ter broken. Tronunel down all day-needed sane welding.
4. Other Comnents: rond created by berm awroximately l/2 full of sediment.
.6.
WJ
Sample
Not
Taken
.J.2.( C)
15:~33
21
0
10
12.4
9
6.5
c(.0.1
1.8
500
170
ll
18:58
17
0
5
llo8
10
6.8
< 0.1
1.7
400
365
August 24, 1981
Time:
Air Temp, °C
Precipitation, inches
Clol.'d COVer, %
Dissolved Oxygen, m;/1
Temperature, •c
~' pH Units
Settleable Solids, ml/1
Flow, cfs
Turbidity, Nro
T. SuspeMed Solids, mg/1
Clem. OXygen Demand, mg/l
Time:
Air Temp, °C
Precipitation, inches
Cloud Cover, '
Dissolved Oxygen, mg/1
Temperature, °C
pi, J:ii Units
Settleable Solids, ml/1
Flow, cfs
Turbidity, NIU
T. SUS{:ellded Solids, .Yl
Chem. OXygen Denand, ng,/1
Time:
Air Temp, °C
Precipitation, inches
Cloud COVer, %
Dissolved Oxygen, m:l/1
Temperature, °C
pi, Pi Units
Settleable Solids, ml/1
Flow, cfs
Turbidity, NTO
T. ~nded Solids, Kq/1
<llem. Oxygen~, ng./1
)
Catments: ;
DEC DEX>NS'l'.RATION PROJEC'i'
FIEID Dt\TA
l
14:24
24
0
5
11.4
8
6.9
0.6
25(!)
60
70.5
1.
i(l
Simple
Not
Taken
ll
10:•6
20
0
5
10.9
8
6.:~
0.4
7.5(E)
700
680
Dry
.a.
WJ
Sanple
Not
Taken
li
15:16
25
0
5
11.1
9
6.8
0.4
27 (E)
120
46.0
SAMPLE UX'ATION
J, .i
12:38
24
0
5
11.7
6
6.9
<.0.1
20(E)
3.2
15.9
1!
15:2.4
14
0
5
10.8
8
6.7
.( {) .1
<0.1
160
144
lLl
Trarmel
Not
Operating
Not
Sluicing
JJl.
10:20
19
0
5
11.9
7
6.,1
70
7.5 (E)
12800
36200
ll
17:52
22
0
5
10.2
10
6e3
<O.l
2.0 (E)
800
875
1. Cubic ya~ moveq/day: Warner: 0; Haskins: 340-425.
Day 50
.5.
14:15
24
0
5
11.6
7
6.9
~ 0.1
3.5 (E)
2.8
5.9
ll.
10:36
20
0
5
10.7
8
6.2
11.0
S.O{E)
3300
1990
ll(C)
18:20
21
0
5
11.0
10
6.1
<0.1
1.8
1100
880
.6.
WJ
Sample
Not
Taken
ll(B)
10:55
21
0
5
11.4
8
6.4
0.2
7.5
700
1070
ll
18:08
22
0
5
10.5
11
6.2
<0.1
1.7
1200
790
2. Equipnent used, hours/day: Warner: D-9 strig;>ing. Haskins: Dragline, 988/4.5 hrs.
3. Problems: Tramel down in the aftemoon-~lding to be done.
4. other Oooments: lOQ-125' of settling pond filled in with sediment. Haskins total sluice
hours for August: 135.5 hrs (Days 29-50); Warner total sluice hours for August: 49.5 hrs.
(Days 29-50) •
APPENDIX IV
To Giani al a
Fulur• Min• Cui -Ditch #I
_....-1---Sample ~ (Trips r and 2)
Gialll { ,~ \ / ump
I tl\h I ~'f \, '~III~! ... ~J Sluice
---'r~ fso· /Runoff \
\
\ r::~/(. ~ (Trip3)
\ Pond #I
""'
"" I \. IG
\
\
\
This Flow Occurrtld ' i {Trip 1)
Dvring Flnl Trip Only \ csooo'
J
l
H \
(Trips 2 and*) • ---
Wat.r Fill•rs Through , " /
Toiling Pil•s \ v / . ,
/ . /
Fish ' ""' ,. CrHir ,""
/
~ :>
~ ::;
l
/
J \ ,,.....//I I
(Trips 2and 3) \ / I 1
ALL TRIPS f I 1 t
NOTE: Distances shown are
alon9 flow linea.
~ J )
Pond #2
Pond #3
Pond #4
Pond#5
Pond #6
,_AM CGNitULTANT8,1NC.
A. Ditch I
8. Ditch 2
SITE
C. Below Sluice and Giant
D. Runoff Entering Tailrace
E. Pond Influent
F. Pond I Effluent
G. 500' Below Pond I Effluent
H. Fish Creek Above Pond 2
J. Fish Creek 250' Below Pond 5
POND AREA
I. 13,300 sq. ft.
2. 18,400 sq. ft.
3. 3,800 sq. ft.
4. 3,100 sq. ft
~-12,900 sq. ft.
6. 10,700 sq. ft.
Total 62,200 sq. ft.
MINE SITE I
FISH CREEK
FAIRBANKS DISTRICT
SETTLING POND DEMONSTRATION PROJECT
DAT.
9-25-81
.CAL. CHIII~:uc•a •v ...... •cw NO• DRAW IN. NO.
NONE RTW 013104 ~-1
--
Hours Sluiced per day: 8
FISH CREEK
MINE SITE tl
FAIRBANKS DISTRICI'
CUbic yards moved per hour: 75-100
Water used: 7.4 cfs 3300 gpm (For sluice and giant)
Water required to sluice 1 cubic yard: Not available.
Equipment used: Giant, dragline, front end loader, elevated sluice box, IJ-8
cat, pump
Wastewater Treatment Method: Multiple ponds built in existing tailings.
Manning Ro~hness Coefficient: -
Dates Sampled: 7/1/81, 7/16/81 and 8/3/6:&.
Description of Operation:
Water is collected :!&:"om the upper part of the watershed in two ditches.
Ditch 1 feeds the sluicebox and Ditch 2 feeds the giant. The giant washes
the mine cut to clear overburden while a loader feeds paydirt to the
dragline which loads the elevated sluice box. To treat watewater the miner
built 6 ponds in existi119 tailings The tailings filter the water as it
percolated towards Fish Creek. When the first pond was full of silt, the
wastewater spilled over into the second pond and so on to the sixth pond.
During the first trip pond one was full,. however the water .had yet to be
directed into the second pond •. On the second trip ponds one through four
were full while pond five was filtering water. During the third trip pond
five was still filtering water. The miner cleaned out each pond at the
beginning of the season and disposed of the silt off site. On the third
trip the miner was stripping overburden from a new mine cut using the giant
and was not sluicing. This site was offstream and important to the study
because of the U$e of existing tailings as a filter medium.
FISH mEEK , MINE SITE 1
SAMPLE SITE Dissolved Water pi Flow, Settleable Total Turbidity
Date SampleCl Oxygen mg/1 Temp oc cfs Solids, ml/1 Suspended Nru
SOlids,ml/1
Trip 1 7/1/81
Ditch 1 12.2 8 6.8 <O.l 17 12
Ditch 2 12.3 10 6.9 <0.1 15 8.2
Below Sluice & Giant 11.3 9 7.2 8.2 4.0 2680 1500
R>nd Influent 10.3 12 7.2 10 7.0 9390 2700
Pond 1 Effluent 10.8 9 7.0 6.4 1.0 2620 2200
500' Below Pond 1 Effluent 10.3 9 6.9 7.1 2.0 2890 2500
Trip 2 7/16/81
Ditch 1 11.7 8 <O.l 13 26
Ditch 2 11.9 8 <O.l 6 5.8
Below Sluice & Giant 12.5 8 8.5 5.5 6870 2900
Pond Influent 9.8 12 9.8 11.5 13800 5600
Fish Creek Above Pond 2 10.7 8 1.5 (0 .. 1 82 40
Fish Cr.. 250 • BelCM Pond 5 10.9 9 6.6 0.2 275 1200
'Jrip 3 8/3/81
Ditch 2 12.2 7 7.1 <O.l 14 45
Below Sluice & Giant 8.2 10 6.3 6.5 70 52600 10800
Runoff Entering Tailrace 11.5 7 6.5 3.2 ( i'!} <.O.l 11 16
R>nd Influent 10.6 10 6.6 10 6.5 5180 1200
Fish Cr. Above Pond 2 10.6 7 7.0 1.9 <0.1 220 700
Fish Cr. 250' Below Pond 5 9.5 8 6.9 6.2 0-8 12 900
Carments: During Trip 2 FH meter was not working. During Trip 3 the Giant was the only machine operating .. It was washing
overburden fran a new. mine cut.
•aM CDN.UL.TANT.,INC.
Foir/Jan!rs
Small FI()W ( CrHK
(Trips2and3) ---.......... ~A~-
~ Storage Pond ~
-Xate
~r----, A~· I \\ I 1w1ne 1 Soil 130
Cut ~~~I
Pump Sluiu
SITE
A. Above Sluice
B. Below Sluice
C. Pond Influent
l,~_,_,,
,. -SmtJII F/tJw ~l_.. fd (rrtps 2 a11d 3) D. Pond Effluent
E. 500' Down~tream Pumps tT' Cu~v•rt Ov.r Tailrace
(Trips 2 ond3) (Trip$ 2 tJnd 3)
\ Pumps
' (rrip I)
1300'
Pond# I
Pond#2
Pond #3
ALL TRIPS
NOTE: Distances shown are alono flow linn.
POND AREA
I. 5,890 sq. ft.
2. 7, 800 sq. ft.
3. 8, 400 sq. ft.
Total 22,000 sq. ft.
NOTES:
I. Two small flOW$ Introduced due to
heavy rains on ucond and third trip.
2. Operotion 80°/o recycle on first trip.
0°/o recycle on second 000 third
trips.
3. On second and third trips ponds
washed out due to heavy rains.
4. Pond #I fu II of sediment on all
visits.
MINE SITE 2
FAIRBANKS CREEK
FAIRBANKS DISTRICT
SETTLING POND DEMONSTRATION PRO" ECT
DAT.
9-28-81
y a..,..ec• •v -ti"...,•CT Na.l DltAWINe NaJ
RTW 013104 3-2
Hours Sluiced per day: 9
FAIRBANKS CREEK
MINE SITE ·t2
FAIRBANKS DISTRICT
Cubic yards moved per hour: 25
Water used: 1.5 cfs 670 gpl'l
Water required to sluice 1 cubic yard: 1,600 gallo~yd3
Equipmen~. used: Dragline, ~rD 444 front end loader, JD 35,0C c;at, sluice box
with conveyor to remove large rock, four pumps.
Wastewate',r Treatment Method: Used three ponds with 80% recycle (miner's
estimate) during first tt:iP. There were· no ponds on the second and third
trips.
Manning Roughness Coefficient: 0.033
Dates Sampled: 6/26/81, 7/14/81, 7/23/81
Description of Operation:
The miner collects water in a storage pond above the site. During sluicing
hours water is released from the storage pond. '!his site uses three IX'nds
in series. During the first trip p;:>nd one was full of silt.. On the second
and third trips all of the ponds were washed out due to heavy rains. The
operation u.ses a dragline to load the sluice box, a front end loader to
remove tailings and a cat for miscellaneous work. The sluice box is on
wheels so it is easily moved as the dragline '~orks up the mine cut. This
site was instream, does not use a grizzly, but does use a conveyor to
remove large rock.
FAIRBANKS mEEK
MINE SITE 2
SAMPLE SI'IE Dissolved Water I1J Flow, Settleable 'lbtal Turbidity
Date Sant>led Oxygen mg/1 Temp oc cfs Solids, ml/1 Sus~nded mu
Soli<JS 1 ml/ 1
Trip 1 6/26/81
Above Sluice 9.8 11 0.4 <.' 0 .1 32 13
Below Sluice 10.9 12 1.2 48 5640 7800
Pond Influent 11.0 11 0.6 55 3600 6600
Ebnd Effluent 9.8 12 0.9 <0.1 776 1100
500; Downstream 9.8 12 0.9 ~0.1 844 1200
Trip 2 7/14/81
Above Sluice 11.2 5 0.7 <:0.1 14 1.0
Below Sluice 10.8 8 1.3 60 24500 1440!1
Pond Influent 10.2 10 2.3 25 23200 8200
Pond Effluent 10.2 10 .2.2 19.0 14800 5600
500' Inmstrearn 10.0 11 2.0 20 15200 7900
Trip 3 7/23/81
'#:x)ve Sluice 10.7 6 6.7 0.9 < 0.1 10 4.6
Below Sluice 8.6 9 6.6 2.0 75 64400 9600
Pond Influent 8.5 11 6.6 2.3 47 33200 9800
Pond Effluent 8.5 12 6 .. 5 2.6 32 25700 8200
500 ' L'ownstream 8.3 11 6.4 2.5 25 26300 7200
Comments: Between first and second trip heavy rains washed the ponds out .• During Trips 1 and 2 pH meter
was not working.
ALL TRIPS
Pond#2
Gilmore
Creek
NOTE: Distunces shown are
along flow lines.
( DAT.
9-24-81
•cAL.
NONE
\
\
~
I •
'
Pond #I
!5001
Ill aM CON aULTANTII,INC'.
SITE
A. Gilmore Creek
B. Tom Creek
C. Below Sluice
0. Pond Influent
E. Pond 1-.. Pond 2
F: Pond 2~ Pond 3
G. Pond 3 Effluent
H. 500' !Jownstream
POND AREA
I. 73,000 sq. ft.
2. 23,900 sq. ft.
3. 15,300 sq. ft.
Total 112,200 sq.ft.
NOTE: Operation is approximately
90 °/o recycle on all tripe.
MINE SITE 6
Gl LMORE CREEK
FAIR BANKS DISTRICT
SETTLING POND DEMONSTRATION PROJECT
----------------------------------------------------------------------------~;~
Hours Sluiced per day: 8
GILM:>RE CREEK
MINE SITE i3
FAIRBANKS .DISTRicr
Cubic yards moved per hour: 90-100
Water used: 6.9 cfs 3100 9}.'E
Water required to sluice 1 cubic yard: 1,900 -2,100 gallons/yd3
Equipnent used: D-8 cat, D-9 cat, nragline, sluice box, pump
Wastewater Treatment Method: Used three pooos, the first one as a pump :f:Ond.
Approximately 90% recycle (miner's estimate) .•
Manning Roughness Coefficit.mt: 0. 022
Dates Sampled: 6/ll/81, 6/30/81, 7/21/81
Description of Operation:
The water collection system is the first J;Orrl, from which water is pumP?d
to the sluicebox. The D-8 and D-9 strip overburden and load the sluicebox.
A dragline removes tailin~s from the sluice b~o~ outfall. There is no
classification of material prior to loading the· sluice. This site used
three ponds, the first pond double.s as a pump pond. The current year's
settling pond is constructed in the previous years mine cuto This is the
only site at which water quality samples were taken between settling ponds.
However, the results show Total Suspended Solids and Turbidity increased
going downstream through ponds one, two and three on trips one and three
and decreased going downstream between the ponds on trip two.. This in-
crease i:S attributed to short circuiting of the pond. The mine was in-
stream and the miner's operation changed remarkably little during the
sampling period.
GniDRE CREEK
MINE SITE 3
SAMPLE SITE Dissolved Water PI FlCM, Settleable 1btal Turbidity
Date Sampled Oxygen mg/1 Tanp oc cfs Solids, ml/1 Suspended mu
S01ids,ml/1
Trip 1 6/11/81.
' Tan Creek 12.3 4 7.6 1.0 <0.1 9 .. 8 55
GilJOOre Creek 12.2 9 .., ~ •• l 0.6 o.o 67 50
Below Sluice 9.4 8 6.6 7.0 14.0 1620 36UO
lUnd Influent 9.5 8 6.7 7.0 12.0 2230 3600
First POnd Effluent 428 1700
Seoond R>nd Effluent 580 1100
Third Pond Effluent 9.4 10 7.3 1.8 <: 0.1 812 1400
500 • Downstream 10.3 9 7.3 1.5 <.0.1 732 1200
Trip 2 6/30/81
Tom Creek 12.2 4 7.7 2.0 <: 0.1 19 7.8
Gilmore Creek 12.4 6 7.4 1.4 <0.,1 5.9 2.3
Below Sluice 12.2 6 7.2 6.8 5.0 2230 6000
~nd Influent 12.1 6 7.0 6.8 4.0 9340 3800
First Fond Effluent 844 2400
Second Bond Effluent 558 1100
Third Pond Effluent 11.9 8 7.8 3.5 < 0.1 468 850
500 • Downstream 11.2 8 7.6 3.4 <0.1 494 700
Trip 3 7/21/81
'Ian creek 12.4 4 6.0 5.3 <0.1 16 3.8
Gil.Ioore Creek 12.9 5 6.5 2.2 <0.1 40 18
Below Sluice 12.5 6 6.0 6.8 7.5 8390 3900
R'>nd Influent 12 .. 2 6 6.0 6.9 8 .. 5 9980 3800
First Pond Effluent 600 840
Second Pond Effluent 1670 2300
Third Pond Effluent 11.9 6 6.0 8.2 0 .. 1 660 1300
500' Downstream 12.2 6 6.2 7.4 <0.1 360 1600
Ccmnentb. ~or the second trip only Gilmore Creek was redirected to enter the tailrace before the first pond.
r
Eagle
Cree.t
TRIP I
Bypass
1000'
NOTE: Dlstoncn shown are alono flow lines.
DAT.
9-29-81
SIT,S
A. Above Sluice
B. Below Sluice
C. Below Tailrace
D. 500' Below Tailrace
E. End of Bypass
MINE SITE 4
EAGLE CREEK
CIRCLE DISTRICT
SETILING POND DEMONSTRATION PROJECT
CNtiGIC.a •v llti!HWBCT NC. a-.WIN. NQ.
RTW 013104 3-4
l
I
f
J I t I I
I
' I . I
II I . I
I
I
f II I
f
ll
l
{
t
i
l
Eagle
Creek
TRIP 2
)
~ I \Bypass
I )~ Pump
I (---~ / . Sluice
\ I ---r-
'
.... ' •so~' __ _, /
Mine 1 H·\f
Cut ( ~
l ~noff[ \
\ / \ l~aoo'
\ l 1-\· .., Mine Site
1 1 t l Not Studied
\
~ I I (No! OpMJ!Ing
1 L--J .J on Date of 7iip)
\l J
r 1
G! I/ l fl
Bypass Wid~ns B~fore
Enmring Et1gl~ CrHk
NOTE: Distances shown are along flow lines.
•aM CDN8U'-TANT8,1NC.
SITE -
F. Above Sluice
G. Ea~le Creek Above End of Bypass
H. Below Sluice
I. End of Bypass
J. 500' Below Bypau
MINE SITE 4
EAGLE CREEK
Cl RCLE Df STRICr
SETTLING POND DEMONSTRATION PROJECT
DAT.
9-29-81
8CAI.. DlltAW
LOS
CN.OIC.D 8V IIIIIICW.GT .NO. .._WINe Na.
NONE RTW 013104 3-e
l
l .._ ____ '""'
1 IIIAM CCN.ULTANT.,INC.
SITE
K. Eaole Creek Above Sluice
L. Below Sluice
M. Bypass Before Tai I race
N. End of Tai trace
0. Eaote Creek 500' Below Tailrace
Min• Sittt
Not Slud.~-.d
(OfJ*rtJftd on Dot• of Trip
Bul Did Not Aff«t Sample S!~ts)
MINE SITE 4
NOTE: Distances shown are alono flow lines.
EAGLE CREEK
CIRCLE DISTRiCT
l DAT.
9-29-81
SETTLING POND DEMONSTRATION PROJECT
.CAL.
NONE
----------------------------------------------------------·~~--------------.
...
Hours Sluiced per day: 9
E.PQ..E CREEI<
MI~ SITE 14
CIRcr.E DIS'IRICT
CUbic yards moved per hour: 90-100
Water used: 6 .a cfs 3000 gpn
Water required to sluice 1 cubic yard: 1,800-2,000 gallons/yd3
Equipnent used: D-6 cat, D-8 cat, dragline, sluice box, panp
Wastewater Treatluent Method: Tailrace
Manning Roll(lhness Coefficient: 0.024
Dates Sampled: 7/2/81, 7/17/81, 7/31/81
Description of Operation:
The miner collects water in a pump pond but does not use it as a settling
pond. The D-6 and D-8 remove overburden from the mine cut and load the
sluice box. Tailings are removed from below the sluice box with the drag-
line. There is no grizzly on the sluice. 'j,lhis operation changed layouts
between each trip, therefore no site averages were made. The mine cut was
moved between the first and second trips. During the third trip water was
p~ped directly from Eagle Creek and the D-~ was removing tailings since
the dragline was not operating. During the second and third trips a miner
tlas set up below this site, r..owever the miner did not affect the sampling
of this site. 'Ibis was an off stream mine.
F..AGLE mEEK
MINE SITE 4
SAMPLE SI'm Dissolved Water PI Flow, Settleable Total 'furbidity
~te Sampled Oxygen mg/1 Tel1p oc cfs Solids, ml/1 Suspended NIU
Solids,ml/1
Trip 1 7/2/81
Above Sluice 11.9 5 12 950 1200
BelON Sluice 12.3 5 37 6350 13400
Below Tailrace 12.5 5 3.0 2870 8600
500 • Bel<M Tailrace 11.9 5 17 4.5 5940 5600
End of Bypass 11.5 6 4.0 6780 6100
Trip 2 7/17/81
Above Sluice 9.4 10 7.0 9.7 0.3 890 1700
Eagle Cr. Above End of Bypass 9.9 12 7.0 1.0 2630 2300
Be1CM Sluice 12.0 3 6.4 15 .. 0
End cf Bypiss 10.0 12 6.9 12 0.5
500' Be1<M Bypass 9.6 12 7.0 1.5 3750 1800
Trip 3 7/31/81
Eagle Cr. Above Sluice 10.8 7 7.2 25{E) 4.0 3940 2400
Bel~ Sluice 11.7 6 6.9 6.8 14.0 18800 3400
B¥Pass Before Tailrace 10.9 8 7 .. 3 9{E) 3.0 4090 3700
End of Tailrace 10.5 7 7.1 18(E) 7.0 3390 2300
Eagle Cr. -500' Below
Tailrace 10.8 7 7.2 48(E) 5.0 5010 3100
Comments: During first trip, the pH meter was not working. During the second trip the operation shut down before
sampling could be canpleted. A miner (not included in this stu~J) set up on the bypass during the second trip
but was not operating. During the third trip they were operating but did not affect sampling. During the th1rd
trip the flow meter broke after the belCM sluice measurement, the ranainder of the flaws are estimates.
~
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\ )
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1 I j~.
I I mine
~ 1 Cui
\ I
Eagle\ \ o./
Cr«rk "\ \ ~
ALL TRIPS
' / A ...._ __ ..,..
' 40'~8 )~m;---~;k;-·\--------
) . . J
( )
\ 1 C (Trip I Onii)
\ ( Tflilroce
""" ) , I
500'
500'
\ lo
'\------+201
\
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500'
·------'-
' E ~
•aM CDNIIULTANTa,INC.
SITE
A. Above Sluice
B. Below Sluice
C. 500' Below Sluice
D. End of Tailrace
E. 500' Downstream
MINE SITE 5
EAGLE CREEK
Cl RCLE DISTRICT
NOTE: Distances shown are alono flow lines.
SETTLING POND DEMONSTRATION PROJECT
DAT.
10· I-81
.CAL.
NONE CH.aiC•D •v 1111110.1.11'1' NU. DIIAWINB ND·
RTW 013104 3-7
EAGLE~
MI~ SITE IS
CIRCLE DISTRICT
Hours Sluiced per day: 2 10 hr. shifts
Cubic yards moved per hour: 80-100
Water used; 11 cfs 4900 gpn
Wa.ter required to sluice 1 cubic yard: 2900-3700 gallons/yd3
Equipnent used: Ir-8 cat, 955 loader, sluice box, PJillP
Wastewater Treatment ~thod: Tailrace
Manning Rouglmess Coefficient: 0.058
Dates Sampled: 7/12/81, 8/4/81, 8/17/81
Description of Operation:
'!his site is downstream of mine site 4. Water is pu~ from Eagle Creek.
~e D-8 cat strips overburden and loads the sluice box while the 955 loader
removes tailings. The operation moved.slightly between trips one and two,
but did not affect the sample sites. The only wastewater treatment was a
1000' tailrace before the effluent re-enters Eagle Creek.
EAGLE CREEK
MINE SITE 5
SAMPLE SITE Dissolved Water Iii Flow, Settleable 'lbtal '1\lrbidity
Date Sampled Oxygen rng/1 Temp °C cfs Solids, ml/1 Sus~nded NlU
Solids,ml./1
Trip 1 7/12/81
Above Sluice 11.6 6 0.4 446 960
Below Sluice 11.5 7 12 15.0 2570 3000
500' Below Sluice 5480 2600
End of Tailrace 11.5 7 11 5.5 5540 3800
500' Downstream 11 .. 8 6 2.8 2500 1800
Trip 2 8/4/81
Above Sluice 10.3 8 7.9 7.0 7460 9100
Below Sluice 10.8 8 7.8 12 15.0 8500 7400
End of Tailrace 9.7 10 7.7 11 9.0 8360 7700
500 • Downstream 11.1 11 7.7 78 alto 5340 7200
Trip 3 8/17/81
Above Sluice 11.& 5 7.4 55 2.5 1560 1900
Below Sluice 11.3 9 7 .. 2 7.8 11.0 7130 1800
End of Tailrace 10.9 10 7.6 13 11.0 7430 5400
500' Downstream 10.9 9 7.4 2.0 2390 2100
COmments: During the first trip the pH meter was not working.
\
\
f-...-t
Bypass/ ""' / /---,t!-~
I. " 'i \ ~a ( Mine l Pump
~ 1 Cut 1
1200'
. ...-j, Washed out
lf-" Pond
,...-----'0
5611/ing Pond
\
Faith
Creek
l
~
I
I
I
j
\
•E \
Prmd Elf/ulnl \ J
Flows f,}v•rland \
5000 t S.ltJr•
R••nlflring Faith " I
CrHk '
""---------l TRIP
SITE
A. Faith Creek Above Pump
B. Bypass to Pond
C. Below Sluice
D. Pond lf'lf I usnt
E. Pond Effluent
Pond Area = ! 85,000 sq. ft.
MINE SITE 6
FAITH CREEK
CIRCLE DISTRICT
NOTE: Distancet~ shown are alono flow linea.""\
SETTLING POND DEMONSTRATION PROJECT
DAT.
9-29-81
I
!
'
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ll
I i
I :
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TRIP 2
Settling
Pond
NOTE: Distances shOwn Cire along flow lines.
DAT.
9-29-81
8CAL!I
NONE
SITE
C. Below Sluice
D. Pond Influent
E. Pond Effluent
F. Fqith Creak By Pump
Pond .Area= 185,000 sq. ft.
MINE SITE 6
Fj~ITH CREEK
Cl RCLE DISTRICT
SETTLING POND DEMONSTRATION PROJECT
·:~ot•atc•D •v •~~~a.~•crr NO• DMWSN• NO·
RTW 013104 3-.9
----------------------------------~~~-----~------------------------------~
TRIP 3
Setlling
Pond
NOTE: Olatancea shown are alonc;a flow lin•.
GAT.
10-6-81
\
-~-
\
SITE
G. Diversion to Pump
H. Below Sluice
J. Pond Effluent
I K. 300 Downstream
Pond Area = 185,000 sq. ft.
MINE SITE 6
FAITH CREEK
CIRCLE DISTRICT
SETTLING POND DEMONSTRATION PROJECT
••o..t•CT NO·
013104
....
H" 1rs Sluiced per day: 11
t Jbic yards IOOved pet hour: 175
FAI'lH CREEX
MINE SITE 16
CIRClE DismiC'I'
Water used: 8.5 cfs 3800 9fltl
Water req.lired to sluice 1 cubic yard: 13 00 gallons/yd3
Equipment used: 0..,..7 cat, D-9 cat, 988 front end loader, 2213 £ront end
loader, pOmp, sluice box with grizzly. ,
Wastewater Treatment Method: Qle settling tx>nd with baffles.
Mcuming Roughness Coefficient: 0.014
Dntes Sampled: 7/6/81, 7/22/81, 8/13/81
Description of Operation:
Water is pumped to the sluice from a pump p:>rd next to Faith Creek. During
the first trip the D-7 and D-9 were loading·the sluice box and the loader
was removing tailings. A new sluice box with a grizzly was installed
between the first and seoond trips. With the new box the 988 loader loaded
the box while the .2213 loader removed tailings. A bypass was routed, on
the first trip only, from Faith Creek into the tailrace below the sluice.
Between the secooo and third trips the mine cut was relocated approximately
1200' downstream. In the new location the sluiee box fed directly into the
p::>nd. The pond has gravel baffles in it to reduce mixing in the pond. The
pond effluent flows approximately 5000' overland before re-entering Faith
Cre-ek. This mine was offstream and was one of two mines to use gravel
baf :les in the settling pond.
FAI'lli CREEK
MINE SITE 6
SAMPLE srre Dissolved water Iii Flow, Settleable 'lbtal 'furbidity
~te Sanpled Oxygen mg/1 Tenp oc cfs Solids, ml/1 Suspended NlU
Solids,ml/1
Trip 1 7/6/81
Faith Cr. Above PLitt> 13.1 7 1.1 ~ 0.1 28 18
Bypass to Pond 12.5 8 7.6 9.0 <.0.1 101 45
Bel~ Sluice 12.4 9 8.2 8.8 12.0 13600 7400
lbnd Influent 12.5 8 7.5 19 s.o 5000 3100
Pond Effluent 11.6 9 7.2 11 0.1 910 1400
Trip 2 7/22/81
Faith Cr. by Plllp 11.5 8 6.7 160(E) <.0.1 12 8.4
Below Sluice 12.0 8 6.3 7o7 16.0 1450 7000
R:>nd Influent 11.0 9 6.3 11 20 14600 6600
lbnd Effluent 10.0 12 6.3 t; 7 "J. < 0.1 870 1500
Trip 3 8/13/81
Diversion to Pump 11.0 7 7.3 5.2 -'0.1 47 45
Below Sluice 10.6 9 6.9 200 15910 ~100
Pond Effluent 10.3 10 6.9 6.9 <: 0.1 1180 1100
300' Downstream 10.2 10 6.8 <. 0.1 1090 2200
Carments: During the third trip the Below Sluice sample site aril Pond Influent sample site were the ~ ..
\
Pump Pond/ S.lfling Pond !"or MiM SiM 9
~
.tJrAp;idl '"\ Qwlt ,,. ~
ALL TRIPS
NOTE: Distancn shown are atono flow II,..
• & M ._,_,._.,.,.N'f'll. INCl.
' -·-
'
SITE -
A. ,.._.ion CrMk Parotfef tc Ptm
•. flaM ly Pwmp
C . ..._ Sluice
D. EMI af TCJitrace
E. Moetoden CrMk ADeM Tailrace
F. Mc.todon CrM 10' ~ TotlrCIOI
MINE StTE 7
MASTODON CA£EK
Cl RCLE DIS'mtCT
SETTLING POND DEMONSTRATION P"OJECT
( .AT8
5·29-81
,.
Hours Sluiced ter day: 11
Cubic yards moved per hour: 60
MAS'ltlX>N <::RED
MINE SITE t7
CIRCLE DismiCT
Water used: 0.7 cfs 300 gpn (miner's estimate)
Water required to sluice 1 cubic yard: 300 ga.llons/yd3
Equipment used: D-8 cat, 275 front end loader, 977 front end loader,
vibrating screen, conveyor, sluice box, •Atley Bowls"
Wastewater Tr~bnent Method: Tailrace
Manning Roughness Coefficient: -
Dates Sanpled: 7/10/81, 7/18/81, 7/24/81
Description of Operation:
The pump for this mine is located approximately 200' downstream of mine
site 19. The 977 loader feeds a hopper which loads the conveyor. The
conveyor dumps material onto a vibrating screen which passes 1• minus
material. '!he material p!S&ing the screen is fed into an agitating chamber
and from there fed into 6 111 Atley Bowls•. On the second and third trips
material passing the screen was fed through a sluice box prior to being fed
into tlle •Atley Bowls." The mine cut was moved between trip t.')ne and two
but did not affect sa•pling. The "Atley Bowls• did not make a marked
difference in the effluent quality. This site was offstr~ The advan-
tage of this method is the low water requirements, as shown by the Below
Sluice flow reading on the RCOnd trip.
MAS'J:(IX)N CREEK
MINE SITE 7
SAMPLE srm Dissolved water PI Flow, Settleable Total '1\Irbidity
Date Sanpled Oxygen mg/1 Tet1p oc cfs Solids, ml/1 SUspended NllJ
Solids,ml/1
Trip 1 7/10/81
Mastodon Cr. Parallel to
Pond 10.4 7 63 0.9
Pond by Ptmt> 11.2 8 325 1200
Be].QW Sluice 12.0 7 19.0 19300 6900
End of Tailrace 10.0 6 6.4 4.5 3670 2000
• Mastodon Cr. 50' BelCM le;l
Tailrace 10.3 7 21 1.3 2680 440
Trip 2 7/18/81
Pond By Pllnp 10.4 12 7.,6 o.a 2180 2600
Below Sluice 11.3 12 6.6 0.8(E) 44 7750 13800
&ld of Tailrace 10.2 7 6.3 5.7 34 3800 10800
Mastodon Cr. Above Tailrace 10.3 11 7.8 2o1 3.0 2180 2800
Mastodon Cr. 50 • BelCM
'!ail race 10.3 9 8.2 14.0 2520 6500
Trip 3 7/24/81
Pond By PlJnp 10.9 10 6.3 0.7 (E) 1.5 1720 3300
Below Sluice 10.1 12 6.5 60 69400 13800
End of Tailrace 9.6 8 6.3 5.2 40 28000 10300
Mastodon Cr. Above Tailrace 10.3 11 6.3 5.5 5.0 4990 2500
Mastodon Cr. 50 • Below
Tailrace 10.6 9 6.4 11 19"0 10900 7800
Comments: For all trips awroximately 80% of the 'flow at End of Tailrace was due to groundwater inflow. During first
trip the pH meter was not working.
n r ;
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TRiP I
NOTE.: Diatonce shown ore alon9 flow 1"'-.
( IINi . I iiX~·
10-2-81 -NON£
)
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(
)
Milltlr
c~
SITE
A. AbcM Sluice
B. Below S4uice
C. Tailrace GAd CrMk Junction
D. 500' OowrAtream
MINE SITE 8
MILLER CREEK
CIRCLE DISTRICT
S£TTLING POND D£MONSTRATI~ Pf'OJ£CT
[Y
MihiJ Cut
_,......,.,.--------~-----........
/"'-\
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Pump
Ponti
-------------. ___ ._,../
Sluic.
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TRIP 2 / Ll NOTE: Distances shown ore along flow lines.
IJ l c ~~~;,
A
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Ar' i
/ Smiling
Pond
•aM •• NI*L.-IIft'8.MIIII.
SITE -
A. AMI Shti.oe
B. 140'. IM<'MJ Sllttint Jitoftd.
C. PoM ly ......
D. a,._
E. 500• Downetreem
Pond Area= 2,400 1q. ft.
MINE SITE 8
MILLER CREEK
Cl RCLE DtST~CT
SETTLING POND DEMONSTIItATION PfltOJECT
r: ! i
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r·
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r·
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JJ .
Milltl Cut
I""_,. - -.._ -._, -· .... ,--. -~-"
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7flllllf,.
Pump/ St1Hiing
Pond Pond
ooo'
• aM CIINiiULTANTII,INC.
SITE
A. Above Sluice
a B.tow Sluice
C. Old Pump Pond
D. Pond By Pump
E. Pond Effluent
F. 500' Downatream
Pond Area = 21, ~50 sq. ft.
MINE SITE 8
MILLER CREEK
CIRCLE DtSTRICT
NOTE: DJttancet shown art along flow linea. SETTLING POND DEMONSTRATION PROJECT
..., ...
RTW 01!104
.l
1
' . 1
Hours Sluiced per day: 8
MILLER OlEEX
MINE SITE 18
CIRCLE orsnu:cr
CUbic yards moved per oour: 150-200
Water used: 11 cfs 5,000 gpn (miner• s estimate)
Water required to sluice 1 cubic yard: 1,500-2~000 gallonsVyd3
Equipnent used: D-9 cat, 966 front end loader, slltice box, pump
Wastewater Treabnent ~thod: Tailrace or pond ( depeniing on trip)
Manning Roughness Coefficient: -
Dates Sampled: 7/11/81, 8/16/81, 9/3/81
Description of Operation:
This operation changed layouts between each trip, therefore no site
averages were made. During the first trip water was collected in an
offstream pump pond, pumped to the sluice b6x and returned to the creek
through a 100' tailrace. The D-9 was loading the sluice while the loader
was removing tailings. During the second ·trip a ne~.~ ;pump pond was used,
while the sluice discharged into a small instream ponc:..i. The same mine cut
was being worked using the same equipnent operation described atove. There
was recycle on the second trip, however the perce."1.tage 'Alas not known. By
the third trip the pump pond and settling pond were connected into one
instream horseshoe-shaped pond. '.Ihe percent recycle on th..~ third trip was
not known. The effluent from the pond filters through tailings" 'nle mine
cut and method of loading the sluice box are the same as during the first
trip.
MILLER <llEF..X
MINE SITE 8
SAMPLE SITE Dissolved water Iii Flow, Settleable 'lbtal Turbidity
rate Banpled Oxygen mg/1 Temp DC cfs SOlidsv ml/1 Suspended mu
Solids,w.J/1
Trip 1 7/ll/81
Above Sluice 11.3 7 1.a < 0.1 1.4 5 .. 4
Below Sluice 7 10.5 8450 3100
Tailrace & Creek Jt.mction 11.2 7 3.7 3600 2200
500 • Downstream 11.4 7 30 5.0 4720 1600
Trip 2 8/16/81
Above Sluice 10.7 9 7.6 5.0 .l 0.1 13 6.4
140' Below Settling Pooo 11.2 9 7.0 15 18 19900 5000
Plm1p Pond 10.8 9 6.8 27 21500 7700
Byp:lss 10.8 9 6,,g 23 21500 5500
500 • ,JX>wnstream 9.8 8 6.6 3.0 36 18200 8600
Trip 3 9/3/81
Above Sluice 10.7 .., 7.6 4.2 ~0.1 3.8 4.4 f
Below Sluice 11.4 '8 7.0 115 8800 2900
Old PtDp Pond 10.6 7 7.6 ,0.1 3.0 320
Ibnd By Pll1lp 11.0 a 7.0 1.6 790 2600
Pond Effluent 12.2 5 7.0 4.7 2.0 2310 2100
500 1 Downstream 11.9 4 7.2 5.1 1.5 1500 1000
Cooments:
l L
\
\
\
\
I
\
\
Pond
£fflutlflt
(Trip$ 2 and 3)
eoo·
H! ALL TRIPS
Min. Cut
Pond £Hiut1nt
(Trip I)
Pump/ S~ffling
PrJnd Pond
Pump Pond lor
MiM Sit. 7
.. -
A. RUMff In Cut
8. Mestoton CNI4(
C. ln••,•nienet Ctelk
0. ~ ly PuMp
E. Below Sluice
F. Peftcl lftflutllt
G. Ptnd Eff I uent
H. MaiN.III C,_. ~· htow Effluettt
flleM Arta = 3, 400 aq. ft.
ftCTE: On oH m,_ ~t:aticn is
opflf Cllif'Mittfy ~ recydl.
MINE StTE 9
MASTOOON CHEEK
CI..CLE OtSTIIOCT
I NOTE: Dis to,_ shown are along flow liftll.
SETTLI. IIONO D£MC*ITfitATION ~JECT
( I ausz.TWim M' l 2 Pi~ W: J 2
. " 013f!4-
Iaiit& --:J 3-15
l
Hours Sluiced per day: 8
MAS'roOON O<EEX
MINE SITE 49
CIRCLE DISl'RICI'
Cubic yards rooved per hour: 150
Water used: 3.2 cfs 1400 gpm (estimated from trip 2)
Water required to sluice 1 cubic yard: 560(E) gallonsVyd3
Equipment used: TWo D-9 cats, two JD 544. front end loaders, a TROJAM loader,
Koering 466 backhoe, vibrating screen, sluice box, pl1Jlp
Wastewater Treatment Method: Settling pond with approximately 80% recycle
(miner•s estimate).
Manning Roughness Coefficient: -
Dates sampled: 7/8/81, 7/25/81, 7/30/81
Description of Operation:
This mine site uses the pump p?nd as a settling pond. Water was diverted
from Mastodon Creek. During the first trip two loaders are loading the
vibrating screen while one D-9 is piling the paydirt for the loaders. The
tailings are removed by the seoond D-9. For the second and third trips the
Koering 466 backhoe was working in the mine cut instead of the cat while
the other machines are in the same places. By the third trip the pump
pond/settling pond was partially filled with silt~ This operation re-
cycles, presorts material and is an example of an efficient use of space.
The effluent from this mine is returned to Ir..dependence and Mastooon Creeks
just above the pump pond for mine site #7.
MAS'ltJX)N amEX .
MINE SITE 19
SAMPLE sr.m Dissolved Water Iii Flow, Settleable '.lbtal Turbidity
Date Sampled Oxygen ng/1 Temp oc cfs Solids, ml/1 Suspended mu
Solids,ml/1
Trip 1 7/8/81
Mastodon Cr. 11.~9 6 24 1.7 1980 1400
Independence Cr. 11.5 7 25 <.0.,.1 36 20
Below Sluice 10.8 5 15.0 6270 4000
a>nd Influent 10.3 5 5.9 6.5 5440 3400
a>nd Effluent 10.8 6 l_S(E) 1.7 1090 1800
Mastodon Cr. 500'
Below Effluent 11.7 6 50 1.0 890 960
Trip 2 7/25/81
Runoff in Cut 9.0 5 0.5(E) ~ 0.1 128 90
f!bstadon Cr .. 10.5 10 6.5 13 1.5 705 900
Independence C:r. 11.1 10 6.5 15 <..0 .1 71 40
lbnd by Pull> 10.0 10 6.6 1.5 3120 3800
Below Sluice 10.8 8 6.5 '35 8890 10800
amd Influent 9.8 8 6.5 3.7 35 6170 8600
R>nd Effluent 9~5 10 6.6 6.3 (E) 5.5 2070 4000
Mastcdon Cr. -500'
Below Effluent 10 .. 4 10 6.7 23 2.5 2520 1900
Trip 3 7/30/81
Runoff in Olt 9.9 3 6.9 0.5 0.1 720 50
Mastodon Cr. 11.3 8 7.7 6.6 0.1 ~111"' J ~ 80
Independence Cr. 10.6 8 7.7 6.·8 (0.1 65 45
l«ld by Pmlp 10.1 9 7.3 1.0 1320 3800
Below Sluice 10.0 9 7.0 240 44900 18800 l R>nd Influent 10.1 9 '7 .1 3.0 160 23500 9900
a>nd Effluent 10.3 8 7.3 2.3 (E) 19 .. 5 l
Mastodon Cr. -500 • I Below Effluent 10.1 8 7.5 9,_7 0.5 129 1300
I I
Cooments: On all trips operation was approximately 80% recycle. Mine S.ite 7 was diverting awrox.imately 1 cfs on the I
I
second trip above Station Mastadon Cr. -500 • Below Effluent.
P'
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ALL TRIPS
F (Trrp I)
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1000' \ ) ~ \ ~rn;,.
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SITe;
A. Above Sf u ice
B. Abet~~ PYm p Pond
C. Pond By Pump
D. lypass
E. ~· Bl&ow Sluice
F. Below SkJice
G. soo' DownltrMf'ft on Bypass
H. End of Tailrace
J. 400' Downatream on Bypass
MINE SITE 10
MAMMOTH CREEK
Ct~LE DtSTRICT L SETl\.ING ftONO DEMONSTRATION ~
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Hours SlUiced per day: 8
~CREEK
MINE SITE tlO
CIRa.E DIS'm!Cl'
CUbic yards moved per hour: 150-17 0
Water used: 7.4 cfs 3300 gpn
water required to sluice 1 cubic yard: 1,200-1,300 gallo~ya3
Equipment used: D-8 cat, two 988 front end loaders, 966 front end loader,
sluioo box, PJI'l'P
Wasta-ater Treatment Method: Tailrace.
Manning Roughness Coefficient: 0. 072
Dates Sampled: 7/9/81, 8/15/81, 8/28/81
Description of Operation:
An offstream pump pond was used to store water. Surplus water and high
flows.are routed through a bypass to protect the pumps and dilute the
sluice box effluent. '!be D-8 cat clears overblrden and piles J:8ydirt for
one of the 988 loaders to feed the sluice box. The other 988 loader
removes tailings. '!be tailrace was relocated between the first and second
trips. '!his was an offstream mine site.
MAMftUlli mEEK
MINE SITE 10
SAMPLE ·srm Dissolved Water :Iii F1Cfi11,. Settleable Total Turbidity
D:lte Sanp1ed Oxygen m;}/1 Temp oc cfs Solids, ml/1 SUs~r.ded mu
SOlids,ml/1
Trip 1 7/9/81
Above Pt:lnp Pond 11.1 9 31 0.5 300 520
Ibnd By 1?\:llp .. 1.0 1240 880
Byp.tss 11.4 9 29 0.3 272 180
Below Sluice 11.8 8 6.7 12.0 1800 3400
&ld of Tailrace 9.7 9 1.1 35 4000 7200
400 • Downstream on Byp&s 10.9 9 38 3.0 .2280 2200
Trip 2 8/15/81
N:Jove Sluice 11.7 7 7.1 11 3.5 2880 1700
Pond By P\ltp 10.8 8 6.9 3.5 6300 33.00
40' Below Sluice 11.1 9 6 .. 0 8.2 18.0 24500 7000
Bypass 10.8 8 6.8 6.0 4.5 4500 5900
500' Downstream on Bypass 10.6 9 6.3 15 14.0 10400 2600
Trip 3 8/28/81
Above Sluice 11.1 8 8.0 35 9.0 6000 3500
R>nd By Ptl1p 10,.8 8 7.8 1.3 2230 2600
40 • Below Sluice 11.0 8 7.6 7.2 27 3180 7400
BypaSs 11.2 9 8.4 19 5.0 1680 2400
500 • Ila«lstream on Bypass 11.0 9 8.3 27 10.0 5320 3100
Catments: During first trip pi meter was not working.
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10-1-81
NOTE: Dittances shown art
okwil f tow lint~.
••• •••s..,L'Mr .... ._.
A.t.iow91uioe ......... ~
c. aalaw Sfuiol
D. K)O' la•w SOui•
E. 1000' .low Stulle
F. 100' .,tPtJ.n ""-"
Eftlill Tef"-
G. c .... CIWil
N. 100• Dz snits zan
MtN€ ~TE II
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Hours Sluiced per day: 8
G(X)KED CREEK
MINE SITE ill
CIRCLE DISI'RICT
Cubic yards moved per hour: 150-200
Water used: 8.9-11 cfs 4,000-S,OQO gpn {miner's estimate)
Water required to sluice l cubic yard: 1,200-2,000 gallonsVyd3
Equipuent. used: Two D-9 cats, 988 front end loader, sluice box, pump
Wastewater Treatment Method: Tailrace
Manning Roughness Goefficient: -
Oates ,Sa-npled: 8/27/81, 9/4/81, 9/15/81
Description of Operation:
This site pumps from an offstream pump pond. The two D-9 cats load the
sluice box while the 988 loader removes tailings. The ground in this area
is flat, therefore the miner does not have room on his claim to get
sufficient drop to build a pond. This was a\"l offstream mine.
CKXJ(ID' <ma:
MitE SI'JE 11
SAMPLE srre Dissolved Water Ill Flow, Settleable it> tal '1\lrbidity ~te 5aupled Oxygen mg/1 Tenp oc cfs Solids, ml/1 SUspended tmJ
Trip 1 8/21/81
So1ids,ml/l
Above Sluice 11a6 9 1.1 74 0.3 165 140 Puq;> Pond 10.2 13 7.,8 1.0 630 1000 100 • Below Sluice 10.0 12 6.9 18 4730 4300 100 • t.Jpetream fran &ld
of Tailrace 9.8 13 6.9 21 6070 6700 500 • Downstream 10.4 13 7.4 7o0 3660 2600
Trip 2 9/4/81
Above Sluice 13.4 2 7.6 34 1.5 1180 1300 Plllp Pond 13.4 3 7.6 1.0 1360 1200 Below Sluice 13.0 5 6.9 80 32300 10800 100 1 Below Sluice 13.2 4 7.0 18.0 11100 5400 1000 • Below Sluice 12.4 6 7 .. 0 12 22 8670 7400 Crooked Creek 12.2 6 7.6 31 0.8 500 400 500 1 bnstream 12.2 6 7.3 49 7.0 3240 2000
Trip 3 9/15/81
Above Sluice 12.6 4 7.2 25 1 .. 0 1210 800 Plmp lbnd 12.4 5 7.3 0 .. 7 995 800 Below Sluice 13.0 6 6 .. 7 50 76700 8600 100' Below Sluice 11.5 6 6.5 14 10500 4500 1000 1 Below Sluice 12.0 6 6.7 15 18 22600 11000 Crooked Creek 11.8 5 7.3 17 0.5 786 2000 500 • lbmstream 11.8 6 7.3 28 5.0 5800 2700
Coxments:
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SITE
A. ~ influent ( Above Sluice)
B. Peftd tty PUMP
C. D•••• C,.. Above Tailrace
D. lelow Sluice
E. EM of T.tlNCI
F. Deadwood Cteek soo' BlkM TaiiMCt
MINE SITE 12
DEADY«XX> CREEK
CIRCLE DISTIIttC"f
IIT'r\Jtlll faOND DIMONI'TMTION ~CT
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Hours Sluiced per day: 8
DP.NXXJ) acE&.
MIE srm tl2
CIRaE DISTRICT
CUbic yards moved per hour: 60-80
Water used: 8.8 cfs 3900 gpn
Mater required to sluice 1 cubic yard: 2,900-3,900 gallonaVya3
.
Equipment used: D-8 cat, two JD 544-B front end loaders, sluice box, vibrating
screen, Plii'P
Wastewter Treatment Method: Tailrace
Manning Roughness Coefficient: 0.010
Jlites Sampled: 7/3/81, 7/19/fJl, 7/26/81
Description of Operation:
The miner u~~es an instream pond for a. pump pond. The D-8 cat pushes
p!lydirt fran the mine cut towards the sluice· tox. One Jlli44-B loader feeds
the washing bin. The paydirt was washed through a vibrating screen into
the sluice box. The other JD544-B loader reaoves t-.ilings. Between the
second and third trip a channel was made diverting water from Deadwood
Creek into the tailrace. turing the sampling period two additional miners
were working Deadwood Creek, cme upstream and one downstream. Neither
miner wu studied nor uaed aettling px1d8. 1bis was an offstream opera-
tion.
DFAIHXD QUE{
MDE SI'l'E 12
SAMPLE sr.n:: Di&SOlved water pi Flow, Settleable Total i\trbidity
Dste Baq>led Oxygen JIQfl 'l'elll? oc cfa Solid&, ml/1 Suspended tmJ
Solida,ml/1
Trip! 7/3/81
Nxwe Sluice 12.2 5 "'0.1 485 48U
Below Sluice 11.9 5 8.0 i,.O 8210 4800
End of 'lailrace 11.5 6 8.0 i.O 500 ssoo
Trip 2 7/19/81
Pond By P\lllp 10.8 g 1.2 2080 1900
Below Sluice ll.7 8 10 13.0 17200 8200
Deadwood Cr. Above Tailrace 10.7 8 17 3.0 6020 1600
&ld of ~ilraoe 10.,6 8 10.0 15100 4200
Deadwood Cr. 500' Below
Tailrace 10.7 8 2.0 2980 1800
Trip 3 7/26/81
Pond By lUip 11.0 10 6.3 0.8 1770 1900
Deadwood Cr. Abwe iailrace 10.1 11 6.4 8.9 1.0 2420 2200
Below Sluice 10.5 11 6.3 8~4 11.0 14900 0000
&ld of Tailr~ce 10.6 12 6.4 11 9.0 12700 6700
Deadwood Cr. 500 1 Below
~ilrace 9.5 12 6.4 19 6.5 7480 5800
Otmmantsz For all tirst and second trips PI meter was not working. During second trip flOW' measurement for
Deadwood Cr. -500' Below Tailrace was taken 400 1 Below Tailrace. Between the second and third trips tart of
Deadwood Cr. was diverted into the tailraceo
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ALL TRIPS
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A.. ., Ill IJ~I.. SktMie
I. llllst htict c.,.. tftftMIIt
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II: toO' DeanaJaealli
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2. 7,JGO ... ft.
3. 1'llOOO ~ ft.
'!lltJ' ToMe t1,410-.ft.
NOTE: Oft tM 1111.-d Nit ,_.#I
.. fwl fl ••••••t.
MiM S"-ltW S1uditltl
(~at t111 DtJt• of Trip 2
IIIII 11M Mill Mllcl $(») .. -..w; MfNE SITE 13
CHENA RIVER
FAtRUNKS Dt! r'ttCT
SETTLINif POND D£MONITM110N fiiiROJECT
NOTE: Olstanoes shown are tiofto flew n ...
1~-----------------~------------------------------~-------J 11 -
Houts Sluiced per day: 8
QlENA ru:VER
MINE sm tl3
FADUWES DISDUCT
CUbic yar.ds rooved per hour: 150-200
water used: 2 c.S cfs 1300 gpm
water required to }lluice 1 cubic yard~ 390-52& gal.l;@fUVlJd3
Equipment used: D-8 cat, D-9 cat, 988 front end loader, baekhoe, vibr:ating
screen, conveyor, tramel, sluice box, ptmp -
Wastewater Treatment Metmd: ~ee settling ponds, the largest one has gravel
baffles.
Manning Rouglmess Coefficient: -
Dates Saq>led: 7/15/81, 7/28./81
Description of Operation:
Water is collected in a pump pond adjacent to a bypass from the Chena
River. A D-8 and D-9 cat remove overburden and pile paydirt for the
backhoe to feed the vibrating screen. The material passin1 was carried by
a conveyor to the trommel. '!he trommel sorts the fines into 4 to 8 sluice
boxes while the coarse fraction passes through. The tailings are removed
by the 988 loader. i~e use of a 900' tailrace and two ponds reduces
settleable solids and total suspended solids before the effluent enters
pond t3. The bypass is routed into pond 13 to dilute the effluent prior to
re-entering the Chena River. This was an offstream mine.
QIENA RIVER
MINE .SITE 13
SAMPLE srre Dissolved Water pi Flow, Settleable 'I\) tal '1\lrbidity
rete 5anpled Oxygen m:J/1 Tenl> oc cfs Solids, ml/1 SUspended N.lU . So1ids,ml/1
Trip 1 7/15/81
Bypass Above Sluice 10.6 9 4.1 < 0.1 1.1 2.6
Below Sluice 11.4 9 2.9 175 44900 16800
Pond Influent 9.2 11 3.0 2.0 24900 13400
Pond Effluent 7.9 13 4.2 ~0.1 660 1800
Before CMma River 8.5 13 2.0 <0.1 25 600
Qlena River 500 • Downstream 2.2 7.8
Trip 2 7/28/81
Bypass Above Sluice 11.3 8 7.4 6.7 ~0.1 25.4 6.4
Below Sluice 12.3 9 7.6 2t.7 40 1160 8900
~nd Influent 9.8 10 7.5 3.4 60 28500 7000
lbnd Efr~luent 9.1 12 7.3 2.5 .(. 0.1 410 160
Before Olena River 9.1 14 7.4 0.1 440 650
Qlena River 500' Downstream 10.7 10 7.4 .(. 0.1 31.0 34.0
Coomstts: 'lbi.s site was sampled only twice. Pond 11 was full of silt during t..~ second trip.
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NOTE: Dtat 1111• lliowft .. 0'-1 f.. liMe.
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RaM a•N-U..1"A.,..,lNC.
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A. Flu.~ CrHk
B. AiM Sluice
C. PoNf by Pu.p.
0. leiow Sluice
E. PaM lnfiUMt
F. POftd EHiut~tt
G. 500• OownMttom
H. tooo• Dowrwtream
Pad. MN:I = 21,000 eq. ft.
NOTE: O,.et4., is QWWOKir.-.ty
so-/o ~.oil tripe.
MtNE SITE l4
flllflMJKS DtSTRtCT
MTYI.IIM ftOND DIMONIT"ATMIN Pfta.I!CT
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Hours Sluiced per day: l.O
FLUME CREEK
M.!NE SITE ll4
FAmBANKS DIS'DUCT
CUbic yards IOOVed per hour: 40-50
Water used: 4.8 cfs 2200 gpn
Water required to sluice l cubic yard: 2,600-3,300 gallons/yd3
Equipnent used: D-6 cat, 2 panps, sluice box
Wastewater Treatment Method: Pump pond used as settling pond
Manning Roughness Coefficient: 0.029
Dates Sampled: 7 /Zl /81, 8/20/81, 8/28/81
Description of Operation:
This site uses the pump pond as a settling pond. The pond was built to
include bushes to filter the water. '!be miner uses the D-6 cat to load the
sluice box and remove tailings.;, This was an instream mine. '!be percentage
recycle was estimated at 800 (m.U'ler's estimate).
FLUME mEEK
MINE SITE 14
SAMPLE srm Dissolved Water PI F1C1tt, Settleable 'lbtal '1\lrbidity
Date Sanpled Oxygen mg/1 Telp oc cfs Solids, ml/1 Suspended NJlJ
Solids,lll/1
Trip 1 7/27/81
Fl\De Cr. 11.0 10 7.0 0.4 1.0 860 500
Pond by Punp 9.4 10 6.~ 0.1 300 600
13elow Sluice 11.0 11 6.9 5 .. 4 10.0 20HOO lObOO
R>nd Influent 11.2 10 6.7 j' .a 10.0 20300 8600
Pond Effluent 10.9 10 6.9 0,.8 0.1 2960 4500
1000 1 Downstrec111 10.7 11 6.9 0.7 (E) 0.1 2300 3900
Trip 2 8/20/81
Above Sluice 14.0 3 6.8 0.2 < 0.1 3.0 4.2
Pond By Ptmq;> 11.6 6 6.8 <0.1 100 150
Below Sluice 11.6 8 5.,9 11.0 15700 8400
Pond Influent 11.6 8 6.0 3.6 33 29400 13400
Pond Effluent 11.6 8 6.0 1.4 4.5 5160 1900
500 1 Downstream 11.5 8 6.0 1.2 4.0 6020 6200
Trip 3 8/28/81
Flune Creek 11.6 10 6.6 0.5 0.2 92 80
Above Sluice 13!92 8 7.0 0.2 <0.1 22 22
Pond By PtJnp 9.4 12 6.1 <Ool 680 1200
Below Sluice 11.5 11 6.2 4.3 40 11600 7700
Pond Influent 11.3 11 5.7 3.8 33 10700 7500
R>nd Effluent 10.2 12 5.6 1.1 6.5 6470 6900
500 1 Downstream 10.3 12 6.0 0.9 4.0 3680 6400
Qmnents: en all trips operation was approximately 80% recycle.