HomeMy WebLinkAboutfeasability wood chip boilerBiomass
Prefeasibility
Study
for
Tazlina
Tribal
Council
Prepared
for
Alaska
Village
Initiatives
with
funding
from
DOE
by:
Alaska
Wood
Energy
Associates
Greg
Koontz,
ME
&
Bill
Wall,
PhD
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Table
of
Contents
SECTION
1
|
Executive
Summary .............................................................................................3
1.1
Background ............................................................................................................................3
1.2
Small
Scale
Chip-‐fired
Boilers ..................................................................................................4
1.3
Project
Scale ...........................................................................................................................5
1.4
Next
Steps ..............................................................................................................................5
SECTION
2
|
Comparisons:
Biomass
Boilers .............................................................................8
2.1
Fuel
Types
and
Handling .........................................................................................................8
Stick-‐wood ............................................................................................................................................8
Wood
Chips ..........................................................................................................................................9
2.2
Batch-‐Fed
vs
Modulating
Boilers ...........................................................................................10
Batch-‐Fed
Boilers ................................................................................................................................10
Modulating
Boilers .............................................................................................................................10
2.3
Integration
of
Biomass
Systems
into
Existing
Systems...........................................................11
Modulating
Boilers .............................................................................................................................11
Batch-‐Fed
Boilers ................................................................................................................................11
2.4
Utilization
Rate
and
Oil
Displacement ...................................................................................12
SECTION
3
|
Comparisons:
Inputs .........................................................................................14
3.1
Resource
Assumptions ..........................................................................................................14
3.2
Resource
Consumption .........................................................................................................15
3.3
Cost
Estimating
/
Project
Costs .............................................................................................16
3.3
Boiler
Performance ...............................................................................................................16
3.4
Benefit
Cost
Ratio .................................................................................................................16
Appendix
1.
P&M
Boiler
Brochure........................................................................................18
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SECTION
1
|
Executive
Summary
1.1
Background
Alaska Wood Energy Associates (AWEA) first published the results of a Level 2 feasibility study on the
subject of biomass utilization in Tazlina in September of 2012. The performance model AWEA uses for
these assessments compares boilers fueled by stick wood, wood chips, and wood pellets. However, one
or more of these fuel sources is often not viable in a village for one reason or another.
Pellets, for instance, are not available off the road system, at least not a price that would be viable. In
other instances, the available biomass end-use equipment itself places a limitation on the viable fuel
types. Biomass boilers are discussed in detail in Section 2, but in the past, the smallest chip-fired AWEA
believed was appropriate for rural Alaska was sometimes simply too large for the application in a given
village. In these cases, a chip-fired boiler could be used, but the cost of the equipment was so high, it was
not financially viable.
This was the case in Tazlina. The four buildings included in the study (collectively labeled the Tribal
Complex) are not large, and even combined into a single heating plant, the heating load was simply too
small for the line of biomass boilers (Wiessmann) that AWEA commonly uses in their analyses. This left
stick-fired boilers, and because Tazlina is on the road system, pellet-fired boilers.
Although smaller in capacity than the smallest Wiessmann boiler, the capacity of the smallest of the line
of stick-fired boilers commonly available in Alaska (Garn) was also larger than the Tribal Complex
required. So, while stick-fired boilers were a better fit than chip-fired boilers, they still had a financial
payback that was excessive (see Figure 1.1 below).
Pellet-fired boilers are available in very small capacities, and therefore it was possible to match a boiler
very specifically to the heating load at Tazlina. Thus pellet boilers showed the best financial performance
of any fuel type; however, the payback of 8.0 years, in conjunction with some of the issues related to
pellets, meant that even the pellet-fired option was not compelling to Tazlina. See Figure 1.1, reproduced
from the original study:
Figure 1.1
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Wood pellets are fundamentally different than stick-wood or wood chips as a fuel; some of these
differences are more relevant that others, depending on the village.
• They are the most expensive form of biomass fuel
• They are highly processed; they are formed from compressed sawdust and wood shavings that
have been mechanically dried
• As such, they cannot be produced locally in small villages, which have no steady source of
sawdust and shavings
Conversely, both stick wood and wood chips are almost always produced locally. They commonly
produce local jobs, help manage local resources, and keep resource dollars in the village.
1.2
Small
Scale
Chip-fired
Boilers
The primary criterion required to re-visit this feasibility study would be a change in some “variable” that
has the potential to make the project significantly more attractive to Tazlina. In this case, AWEA
believes that the availability of a viable small scale chip-fired boiler meets this criterion.
The key word is “viable” – small chip-fired boilers do exist, and have for many years. There are two
primary reasons that AWEA did not consider the ones they were aware of as “viable” for use in rural
Alaska:
1) They require wood chips with a moisture content of 35 percent (MC 35) or less. Wiessmann
has two “model lines” or series of chip-fied boilers. The smaller series has a boiler that a
capacity that would fit the Tribal Complex well – but the boilers in the smaller series require
chips with MC 35 or less. Other smaller chip-fired boilers would not operate even at MC 35.
It is possible to achieve MC 35 chips in rural Alaska, even without mechanical drying.
However, it requires air drying for extended periods of dry weather, which are often few and far
between. In addition, if something happened and the “dry chip” supply ran out, it could be
weeks or months before a new supply of MC 35 chips was available. This is not an acceptable
premise on which to building a new heating plant.
2) They were not sufficiently automated. In order to be a viable solution for a replacement to an
oil boiler, ideally the boiler should be as easy to use and automatic as the oil boiler. No chip
boiler quite meets this criterion, but at a minimum, AWEA requires that a chip-fired boiler:
a) auto-start the boiler when heating demand requires heat
b) modulate the fuel and air to maintain the hot water temperature
c) be robust and simple to fix
As they get larger and more sophisticated, chip-fired boilers often incorporate additional
features that make them even more convenient and efficient – but AWEA considers the short
list above to be the minimum requirements.
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The reason for re-visiting the Tazlina study, therefore, is that AWEA has become aware of a
manufacturer with a newer line of small scale chip boilers that we believe meet these criteria. The State is
also interested this new line of boilers, and the first one in Alaska is scheduled to be installed in Mentasta
Lake soon.
The manufacturer of this boiler is Portage and Main (P&M), of Canada. Their line of chip-fired boilers is
called “EnviroChip”. There are two boilers models in the line, the 500 and the 800; however, the 800 is a
custom unit, and not UL listed, so only the model 500 will be considered here.
Again, boilers are covered in detail in Section 2; The P&M 500 is covered in more detail there. The
purpose of this revised report is to determine how the application of this boiler would affect the
economics of a biomass heating project in Tazlina.
1.3
Project
Scale
As noted above, there were four buildings included in the original study, as there are in the revised study.
The performance model AWEA uses automatically evaluates each building for an individual boiler, and
then evaluates any grouping of buildings that the user chooses. In the case of this revised report,
however, we are going to look only at a biomass heating plant that would include all four buildings; the
Tribal Complex. Figure 1.2 below shows the four buildings that comprise the Complex, and their current
annual oil consumption:
Figure 1.2
1.4
Next
Steps
A number of things have changed since the publication of the original report, not least the emergence of a
viable small-scale chip-fired boiler. There are three further Sections to this revised report, each deals with
comparisons; these Sections elaborate on these changes in detail. One that deserves mention here is that
as AWEA spends more time working in rural Alaska, we learn more about construction practices and
costs in rural Alaska, and of course, material and fuel costs change constantly. Thus the economics
presented here for stick and pellet-fired boilers will not match exactly the figures from the original report.
Sections 2, 3, and 4 provide additional information on these changes.
The P&M boiler represents such a significant change to the project viability for three reasons:
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1) It can operate with wood chips up to MC 45.
2) The boiler is the “right size” for Tazlina, and while it meets the chip-boiler criteria above, it is
simple and robust; this is reflected in a first cost that is much lower than any boiler in the
Wiessmann line.
3) It automatically attempts to re-start based on a timer – if the boiler is still running, nothing
happens. However, if the flame has “gone out” due to low load, it will re-start. This combined
with thermal storage (see Section 2) means that it can usefully cover any load from zero to the
maximum listed capacity – this maximizes the amount oil that can be displaced.
Figure 1.3 below shows both the old and new results, side by side (the “old” results are replicated from
Figure 1.1 above). From this point in the report going forward, results from the original report will be
grayed out, while new results are in black.
Figure 1.3
The “B6” (or Building 6) in the title block of both tables reflects the fact that the combination of the
buildings occupies the sixth position in the analysis model (see Figure 1.2) – it has no other significance.
For the stick-fired and pellet-fired options, the financials have gotten slightly better (nothing changed
except some of the underlying resource and cost estimating assumptions, as noted above). For the chip-
fired option, however, the use of the P&M 500 boiler reduced the net simple payback (NSP) by almost a
factor of four. In this revised study, it emerges as the best option based on financial considerations.
Because it uses wood-chips as a fuel, it also provides some of the additional benefits associated with
wood chips listed above.
Figure 1.4 provides additional project detail, for the chip-fired boilers only, with a comparison between
the first analysis and this update of the report.
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Figure 1.4
The three key values to take from Figure 4 are:
1) The P&M boiler displaces 100 percent of the oil vs about half for the Wiessmann; this
significantly increases savings
2) The “revised” boiler-associated costs drop from ~$163,000 to ~$34,000.
3) The amount of wood chips (and harvest acres) required in the revised model more than doubles
from the amount in the original model.
The increase in wood-chips required is almost entirely due to the fact that in the revised model, the boiler
displaces all of the oil, as opposed to about half. However, it must be said that the P&M boiler is
significantly less efficient that the Wiessmann boiler (0.77 vs 0.85 – may not seem “significant, but it is).
We encourage Tazlina in their fuels reduction practices to harvest both hardwoods and spruce and allow
drying for one field season. This will reduce the moisture content by at least 20% bringing chip moisture
to about 30%. This significantly increases the recoverable BTUs per ton of chips and allows the needles
and leaves to fall off and out of the product stream going into the boiler. Two additional pieces of
equipment will be required but have not been put into the financial models. These are a small commercial
knife type micro chip chipper and a small bobcat for loading the hopper. There is so much variability in
the opportunities for tribes to secure this equipment that we did not model it in the financials. However,
the project has such strong financials that these two pieces of equipment will not significantly impact the
benefit cost ratio.
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SECTION
2
|
Comparisons:
Biomass
Boilers
2.1
Fuel
Types
and
Handling
Stick-wood
Stick wood consists of lengths of wood, cut to the length of the furnace or fireplace they are intended for.
If the diameter of the wood is too large for the application, then the wood is split into pieces – this
improves the burn and allows the use of larger wood. The standard unit of by which stick-wood is sold is
the cord.
In the lower 48, wood is commonly gathered, cut and split in the summer, and then covered and
stockpiled for the winter. This allows the wood to “season” – it dries out and thus produces a cleaner,
hotter burn. The useable heat content (BTU/lb or BTU/cord) increases as the moisture content drops.
In rural Alaska, however, the scenario is often different. First, the heating season is much longer, so the
amount of wood to be gathered is much larger. Second, access to wood is generally better in winter after
the freeze begins than it is in summer. For that reason, stick-wood in Alaska is not likely to be as dry as
it is in the lower 48, and will not burn as hot or clean.
In terms of material handling for a boiler, stick-wood is handled manually. No one has yet come up with
a small-scale boiler than can automatically feed stick-wood, in all its variations, into a boiler. While this
manually feeding means there is no chance of a material handling failure, it requires a significant amount
of labor (see below). It also affects how stick-fired systems operate (Section 2.2) and integrate with
existing systems (Section 2.3).
There is another aspect of stick-wood that affects local resources in rural Alaska – it can difficult to fully
utilize the available wood resource. The furnaces into which stick wood is fed are cylindrical, and the
diameters are not overly large – 25 to 40 inches for the line of boilers AWEA typically evaluates. The
recommended wood diameter for these furnaces is 3 to 12 inches. While wood that is larger than 12
inches in diameter can be split, wood 3 inches and below constitutes a significant fraction of the wood
resource that cannot easily be used. Smaller sections are also often highly branched, which makes
loading the furnace very difficult unless the branches are manually stripped into more or less straight
pieces.
AWEA utilizes one line of stick-fired boilers in their analyses; the line manufactured by Garn. There a
number of Garn boilers in Alaska. Garn has three sizes of boilers, detailed below.
Pellets: Wood pellets are mechanically dried sawdust and shavings that are mechanically compressed
into evenly sized pellets. They have extremely low moisture content (MC 5 or less), and are thus very
“energy dense”. They all virtually smooth, uniform in size, and thus “flow” almost like a thick liquid
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when handled. They almost never foul a material handling system – in some respects they are an ideal
biomass fuel. Because of the low moisture content, the efficiency of pellet boilers is exceptionally high.
Wood pellets are sold by the ton; in this case, the moisture content is so low that no one distinguishes
between green tons and dry tons.
However, the amount of processing required to make the pellets means they are expensive. The “raw
materials”, sawdust and shavings, are a generally the byproduct of lumber industry, the furniture industry,
or both. For that reason, pellets are not generally produced in rural Alaska because almost no villages can
produce the steady stream of sawdust and shavings required. Any village that uses them must therefore
be on the road system, so that the pellets can be trucked in.
Because of the high cost of pellets compared to chips, pellet-fired boilers are generally not manufactured
in very large sizes – once the boiler gets to a certain size, the assumption is that the user is sophisticated
enough to deal with wood chips, which are a cheaper fuel on a unit basis. Thus pellets boilers are
generally designed for much lower capacities than chip boilers. The Froling P4 line of pellet boilers
ranges in capacity from 35 to 200 kBTU/h in heating capacity – the Pyrotec line of Wiessmann chip-fired
boilers ranges from 1,331 to 4,265 kBTU/h.
Wood
Chips
In some respects, wood chips represent for rural Alaska a biomass fuel combination of some of the best
aspects of stick-wood and pellets, and avoids some of the negative aspects:
• Unlike stick-wood, virtually the entire wood resource can be chipped; this minimizes
harvesting labor, transport cost, and resource wastage.
• At the same time, chips can be produced locally with minimal processing; harvesting can be
integrated into local resource and fire suppression planning, and collection and processing can
increase local employment.
• The cost is comparable on BTU basis to stick wood – is generally higher, but not by much.
• Unlike pellets, chips do not rely on associated industries for the raw material; chips can be
made from slash, trimmings, whole logs, clean construction debris, etc.
• Chips handle almost as well as pellets – the more uniform they, the better they handle. This
makes them appropriate for automatic feed systems such augers, etc. that allow the boiler to
modulate to meet load (see next section below)
• The minimum amount of processing required is the chipping itself. The P&M 500 boiler is
designed to work well with a 2” minus chips (edge length in all three dimensions is 2 inches or
less), but can handle variations in that spec.
• In terms of handling, the issues that cause jams and failures are overs (generally long, stringy
fibrous pieces) and saw dust (especially when wet, it can clog and jam systems). These can
virtually eliminated by adding one step to the process; screening.
Wood chips are sold by the ton, either green (GT) or bone dry (BDT). One ton of MC 50 wood chips
equal 1.0 GT and 0.5 BDT – half of the weight is water and half is wood. Although wood chips are
generally sold by the BDT to avoid the effects of variations in moisture content, in rural Alaska we are
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generally dealing with villages that harvest and process their own chips; they are not “sold” to a third
party. For that reason, in our analyses, AWEA uses green tons, and we specify the wood specie(s) and
moisture content of the chips. Because Tazlina is on the road system, they could in fact buy chips from a
third party (and likely would do so) – but we still base the analysis on GT.
2.2
Batch-Fed
vs
Modulating
Boilers
Batch-Fed
Boilers
The stick-wood fired boilers used in rural Alaska are batch-fed. The operator cleans out the ashes from
the previous batch of wood, fills the furnace with wood, lights it, and waits for that “batch” of wood to
burn. Garn indicates that a “burn” generally lasts 30 – 60 minutes.
The heat from this burn must go somewhere, and because the burn rate does not depend on the actual
heating load, there must be a means to store the heat. The furnace of a Garn boiler is surrounded by a
large, integral water tank. The size of the furnace (and thus the amount of heat from the burn) is designed
to heat the tank from a lower temperature to a higher one; in the case of Garn, the design is intended to
raise the tank from 120 deg F to 200 deg F.
The heating system pumps hot water from the tank to the building heating system as needed to meet the
heating load, and returns cooler water (though still warm) to the tank. Thus the tank temperature
gradually drops. When the tank temperature approaches 120 deg F, it is up to the operator to determine
this is the case, and start a new burn. If this new burn does not occur, eventually the tank water gets too
cool for the heating to use.
This is a batch process, and the “control” (the rate and timing of burns) and material handling (feeding
stick-wood) are entirely manual. The implications of variable temperature water to the heating system
and of batch-fed fuel are discussed further in the 2.3 and 2.4.
Modulating
Boilers
By contrast, modulating boilers systems have the ability not only to automate the feeding of fuel to the
boiler, but also to vary the rate of fuel feed in response in the heating load. Within relatively tight limits,
they maintain a constant hot water temperature. The set point for this hot water temperature can be
changed with the seasons; but whatever the set point, a modulating boiler will regulate the fuel and air
within the limits of the unit to maintain that set point. Chip-fired and pellet-fired boilers are modulating
boilers.
Because they modulate fuel to meet heating load, theoretically modulating boilers do not require any
thermal storage (a water tank). However, even modulating biomass systems work best if they have some
storage. Biomass boilers can only modulate output so fast – once the wood is on fire, it will eventually
burn even if the heating load is decreasing. Conversely, when a surge in heating load occurs, it takes time
to get new wood into the furnace and get it burning; a water storage tank helps the system even out these
rapid load fluctuations. Finally, if the load gets so small the boiler shuts itself off, the tank takes up the
slack unto the boiler auto-restarts. By combining a modulating boiler with sufficient thermal storage, one
gets a system that modulates to handle any load from virtually zero up the maximum capacity of the
boiler.
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2.3
Integration
of
Biomass
Systems
into
Existing
Systems
Modulating
Boilers
Oil-fired boilers are the norm is rural Alaska; these are modulating boilers that regulate the flow of oil to
the burner to meet the hot water set point. Integrating a modulating biomass boiler into an existing oil-
fired system is therefore simple.
In the simplest form, one would simply install the biomass boiler in series with the oil-fired boiler(s), and
upstream of the oil-fired boiler(s). This means that the cooler hot water return water from the heating
system flows through the biomass boiler first, and then through the operating oil-fired boiler. Then one
would stagger the boiler hot water set points.
If the minimum hot water temperature required is 170 deg F, for example, the biomass boiler set point
might be set at 180 deg F (water hotter than required causes no harm), and the oil-fired boiler set point
would then be set at 170 deg F.
As long as the biomass boiler has fuel and is functioning, it will generate 180 deg F water. Even if rapid
load fluctuations cause the hot water temperature from the biomass boiler to vary, it would take a 10 deg
F deviation to start the oil-fired boiler. In other words, as long as the hot water temperature from the
biomass boiler is at least 170 deg F, then the oil-fired boiler will not fire – the “return” water is hotter than
or equal to the supply set point, so the boiler does not fire. If for any reason, the biomass boiler fails or
the heating load exceeds the capacity of the biomass boiler, then the hot water will drop below 170 deg F
– at which point the oil fired boiler starts, and fires as required to maintain its own set point of 170 deg F.
This is completely automatic and requires no operator intervention, and as long as the oil-fired boiler does
not fail, it is fail-safe. The end-users would not even realize it had happened – they would still be getting
hot water and heat.
There is second, equally important implication of this set-up. Biomass boilers are expensive compared to
oil-fired boilers. The goal of most biomass systems is to displace most, but necessarily all of the oil
consumption in the selected buildings. If a biomass boiler can cover the heating load for 90 percent of the
hours in a year, it probably makes no sense to buy the next bigger unit just to cover that last ten percent of
the annual hours.
The setup above allows one to size the biomass boiler based on the best combination of price and size.
As noted above, if the installed boiler cannot keep up with the heating load, the hot water temperature will
fall until it falls enough to start the oil-fired boiler, which will then make up the small amount of load the
biomass boiler cannot cover. Because the biomass boiler “sees” the return heating water first, it will load
up to 100 percent, and only then will the oil-fired boiler come on – the use of biomass is always
maximized without having to size the boiler for 100 percent of the worst case heating load.
Batch-Fed
Boilers
The set-up above is not practical with batch-fed boilers; they burn fuel without regard to the actual load,
and store the excess heat in the surrounding hot water tank. Between burns, the tank temperature drops as
low as 120 deg F before the next burn. If one attempted the same series boiler arrangement described
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above with a Garn boiler, the oil-fired boiler would come on at 170 deg F, and the remain on until the
next burn raised the tank temperature above 170 deg F – meanwhile, only 3/8ths of the heat of the
biomass burn would have been utilized: (200 – 170) / (200 – 120) = 3/8. One could set the set point of
the oil-fired boiler at 120 deg, except that in winter 120 deg F water is almost certainly not hot enough to
allow the system to heat the building spaces.
So a batch-fed biomass boiler can be set up in fail-safe mode upstream of an oil-fired boilers, but as the
example above shows, the result would be that the utilization rate of the biomass boiler decreases
significantly (see 2.4 for an explanation of utilization rate), and the resulting annual oil consumption for
the building or buildings would be much higher than in a modulating boiler system.
2.4
Utilization
Rate
and
Oil
Displacement
Utilization rate is a simple concept. A village pays for a piece of equipment, perhaps an expensive
biomass boiler. Ideally, that equipment would run at 100 percent of capacity, 100 percent of the time – a
utilization rate of 100 percent. Assuming the piece of purchased equipment is intended to save money,
then the it would seem that the higher the utilization rate, the higher the return on the investment.
However, in the case of a biomass boiler, there is a second factor that figures into the return on
investment – how much oil consumption (as a fraction of annual consumption) does the biomass boiler
displace. After all, this is how the biomass boiler generates savings, so oil displacement has to factor into
return. In fact, sizing the biomass system to maximize return on investment is a balancing act between
utilization rate and oil displacement.
Figure 2.1 helps explain how utilization rate (UR) and oil displacement (Disp) influence savings and
return on investment:
Figure 2.1
The Y axis is the percent of full heating load, and the X axis is the percent of the annual outside air
temperature (OAT) range. If the village outside air temperature varied from -40 to 60 deg F in a year, the
range would be 100 deg F, and each 1% would correspond exactly with a 1 deg F change in OAT. The
point is that at 0.0 on the X axis, that is the coldest OAT, and at 1.0 on the X axis, that is the hottest
temperature in the village.
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The thick red line is an idealized heating load curve – as temperature rises, load decreases. At some OAT
(assuming that domestic hot water (DHW) is being heated by the boilers), the space heating load
disappears and only the DHW load is left (the flat portion of the load curve).
The dashed blue line is the capacity of the biomass boiler, expressed as a percent of the maximum heating
load.
In the first graph, our “first attempt” at sizing the biomass boiler was to start with a biomass boiler that
was quite small – the capacity is only 15 percent of the max heating load. As a result, the utilization rate
is very good; we have almost achieved the goal of running the boiler at 100 percent of capacity 100
percent of the time.
However, the system achieves very little displacement of oil, and thus not much in the way of dollar
savings. This can be seen by looking at the area above the dashed blue line and below the red load curve;
this is the portion of the heating load served by oil. In a purely oil-fired system, all of the area below the
red line represents oil. In our first attempt, then, we have not really displaced very much of that oil,
despite the very high utilization rate. Since displacing oil is what generates the dollar savings needed to
pay for the boiler, we have not maximized the return on investment.
In the second graph, the sizing of the boiler is taken to the opposite extreme. In this case, we have
displaced all of the oil, except for the tiny triangle in the upper left – too small to even label it as “oil
heat”. However, our utilization rate has dropped to about one-half; half of the boiler capacity we paid so
much for sits unused over the course of the year.
If we assume that the cost of wood is relatively stable, and the cost of the biomass boilers changes over
time, but only slowly, then the “correct” balance between utilization rate and oil displacement depends
almost entirely on the cost of oil in the village. A higher cost per gallon for oil argues for more oil
displacement – the added savings can pay for the unused capacity. A low cost of oil argues for a higher
utilization rate – better to minimize unused capacity and run the boiler as close to 100 percent as possible
at all times. AWEA evaluates these factors in every village we work with to get the correct size of boierl
This simple analysis explains why the availability of the P&M 500 boiler changes the economics of
biomass heat so significantly for a village such as Tazlina. Although the P&M boiler can in this case
displace in excess of 99 percent of the oil normally consumed in the Tribal Complex, the amount of
excess capacity Tazlina would pay for is small enough that the savings from the oil can pay back the first
costs in a reasonable amount of time. In the original analysis, the smallest available chip-fired boiler was
so much larger than needed that even with 100 percent oil displacement, the savings could not pay for all
that excess capacity.
The examples above assume the biomass boiler runs whenever it can, as hard as the heating load allows it
to run. There is one condition under which a lower utilization rate is unambiguously bad; when the
biomass boiler is not running when it could/should be. In such a case, utilization rate drop and oil
displaced drop at the same time – the oil fired boilers are running when the load could be met with
biomass.
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If this occurs due to a mechanical failure, then not much can be done about it, except to fix the problem as
fast as possible. If, however, it is a function of the biomass boiler or the biomass system, then it is worth
examining whether the biomass boiler selected is the best fit for the application.
The best example of this is the application of batch-fed boilers. The rate at which heat is extracted from
the integral water tank varies with heating load, and thus with outside air temperature. On a hot day, a
single burn might be sufficient for the whole day, or even two days. On a very cold day, the tank might
have to re-charged four or five times a day. Ideally, a burn takes place right as the tank temperature
reaches about 120 deg F, but the only way to know when that happens to manually check a thermometer
(which could indoors, on a pipe, or outdoors, at the tank).
Obviously, some if not most of the burns required to maintain tank temperature will occur at night, when
it is very cold. As noted before, this means manually cleaning the ashes of the previous burn, and loading
lighting the new fuel. Given the fact that the biomass system is backed up by oil, the temptation to skip a
few burns or one per cold night will be very high. In such a case, both utilization rate and oil
displacement drop, and the payback period on the biomass boiler gets longer. The higher the cost of oil
per gallon, the more effect such lapses in utilization have on the project economics.
SECTION
3
|
Comparisons:
Inputs
3.1
Resource
Assumptions
The primary resource assumptions that must be made about any existing or proposed fuel are A) the cost
of the fuel per unit, and B) the heat content of the fuel per unit.
In terms of cost, the assumptions were slightly modified. The cost (and heat content) assumed for No. 1
oil did not change from the original analysis, so only one version of this table is shown in Figure 3.1
below:
Figure 3.1
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For stick-wood and pellets, the assumed costs remained the same. For stick wood and wood chips,
however, the heat content was assumed to be slightly lower in the revised report than in the original. In
the original analysis, it was assumed that some of both the stick-wood and chips could be obtained at an
average moisture content of 30 percent (MC 30), with the remainder at MC 35. In the revised analysis, it
was assumed that all of the stick and chip fuel was at MC 35 – this slightly lowered the net useable heat
of the fuel, and increased the number of cords/green tons required to generate the same amount of heat.
At the same time, the cost of chips was revised based on more current data. The following tables (Figure
3.2) show both unit costs of the various fuels in the unit which they are sold, but also the unit costs in a
common unit, millions of BTUs (mmBTU, as above):
Figure 3.2
Even with a unit cost wood chips that is 50 percent higher than in the original report, with the use of the
P&M 500, a wood-chip based system now has the best payback.
3.2
Resource
Consumption
The primary resources consumed by the existing and proposed project are oil and wood for fuel. A
secondary resource, in terms of system cost, is electricity. Figure 1.4 above shows the relevant data for
oil and wood chips, original and revised.
In the original report, the chip fired boiler displaced only about one half of the current oil consumption
4,086 gallons displaced out of 8,078 gallons total). This is because A) the Wiessmann boiler was much
too large for the application, and B) we did not assume thermal storage, which allows the boiler to handle
low load conditions. The chip-fired option was already quite expensive, and the larger the boiler, the
more thermal storage is required, and the more than costs, and so on. With the P*M 500, the boiler is a
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better fit for the load to start with, and we did include thermal storage, so oil displace was 99 plus percent
– only on an extremely cold Tazlina day would supplemental oil heat be required.
In terms of wood chip consumption, as noted above, consumption increased due to three factors – in order
of magnitude: 1) doubling the amount of oil displaced requires basically doubling the amount of wood
consumed, 2) the P&M 500 is about 10 percent less efficient than the Wiessmann boiler, and 3) our
resource assumptions slightly lowered net useable heat per ton of chips (see above). This resulted in an
increase to 116.4 green tons per year from the original estimated of wood chip consumption of 51.3 GT
per year. The figures for required acres of forest harvest are 7.76 and 3.49 acres per year, respectively.
3.3
Cost
Estimating
/
Project
Costs
Leaving aside the obvious fact that the P&M 500 cost much less than the smallest Wiessmann chip-fired
boiler, the cost estimating has not changed much between the two reports. Some line items have gone up
in cost, others have come down, and for still others, we have better definition or more information on
which to base our estimate. In general, however, both the stick-fired and pellet-fired options have
increased since the original report by just about the amount one would expect based purely on inflation.
The actual values of some of the larger project cost line items (original and revised) can be seen in Figure
1.4 above.
3.3
Boiler
Performance
The performance of the Garn (stick-fired) and Froling (pellet-fired) boilers has not changed since the
original report. There are some differences between the original Wiessmann chip-fired boilers and the
P&M 500 boiler.
The Wiessmann is a more sophisticated, more automated line of boilers. They include automatic de-
ashing, for instance. They can incorporate external emissions controls, such as flue gas recirculation
(reduces NOx), and multiclones (reduce particulates and soot). They has a programmable control panel
which has options to automatically include thermal storage in the control sequence, as well as integrating
solar hot water (if available). It has more heating surface area per input BTU, so it is more efficient than
the P&M 500.
However, as noted above, the P&M 500 meets the primary criteria for installation in rural Alaska, the
ability to auto-start (and re-start) the ability to modulate fuel and air to maintain a hot water set point.
Thermal storage can be accommodated, but it must be done using external controls. The P&M is simpler,
and slightly less efficient, but it nonetheless fits very well into the niche of a small scale chip-fired boiler.
3.4
Benefit
Cost
Ratio
The benefit to cost ratio is an attempt to capture the value of the project over the lifetime of the project. A
lifetime of 20 years is commonly used. The output of the calculations included is actually two numbers,
the actual benefit/cost ratio, and the net present value (NPV) of the project.
The project cost is a one-time event, but the savings accrue over the life of the project. Depending on the
assumed inflation rate of the various fuel sources, the savings may actually increase each year (if, for
instance, oil rises faster than biomass, as we have assumed). On the other hand, a dollar saved in year 20
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is not worth a dollar today; it is worth the NPV of one dollar, at the assumed discount rate. The discount
rate is the rate of return one assumes one could make if that dollar were invested in some other fashion –
in a bank account, or on another project. The combination of one time and recurring costs, plus inflation
and discounting means that it would be very useful if the lifetime benefits, divided by the lifetimes costs,
could be boiled down to one number; the benefit to cost ratio.
The current year is always year zero for the calculation, and it is generally assumed that construction
would be completed in year one (or, for a long process or project, year two). The NPV of the project cost
for a project completed in year one is almost, but not quite the same as the project cost; it has only been
discounted one year. This is the COST part of the ratio. The BENEFIT is the NPV of the stream of
savings (fuel savings, in this case) that the project generates over the 20 year lifetime. Divide the Benefit
(in dollars) by the Cost (in dollars), and you get the dimensionless Benefit to Cost ratio; generally, any
value over 1.00 is considered good, but different agencies have different target values.
The NPV benefit is simply the NPV of the combined (savings minus cost) Cost and Savings cash flow
over 20 years. In the year the project is constructed, the “savings stream” is negative, because the
discounted project cost is much greater than the yearly savings – all other years, the savings are positive.
Take the NPV of that cash stream, and that is the NPV benefit of the project. Unlike the ratio, this value
only really tells one something useful when compared to another variant of the same project, or another
project that would use the same initial cash input. The project with the higher NPV benefit (in dollars) is
generally better.
Figure. 3.3
Figure 3.3 demonstrates a very positive Benefit Cost ratio of 3.57 and a NPV net benefit of $446,378.
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Appendix
1.
P&M
Boiler
Brochure
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