Loading...
The URL can be used to link to this page
Your browser does not support the video tag.
Home
My WebLink
About
Appendix 5
1-07-N 115:U From-Ala6ka Anvil. Inc DOt-iTD-a0$9 T-767 P 001/014 F-005 qqlrALASKA ANVIL INCORPORATE] Innovative Engineering & Technical Services 509 West r Avenue Mcharage, Alaska 99501 (907) 276-2747r www,anvikorp.com Facsimile DATE' 517103 TO: Jason Wells Valdez Fisheries FAll h�. 907-835-4831 NU Of PAGES (1nauain; mis sh=0 1 of 14 MWM' Barb Grisham rXT 3076 Dom: Admin. FAX NO. Anchorage, 907-2794088 EWIL ADDRESS: NOR.MA1.. ® L;PCE-IT ❑ CONFIT)F TLUL ❑ 5LVE•C7: Conceptual Engineering letter PR03ECT NO-. Cc: Project File �ICUESK-n%MENT5: Here is the Conceptual Engineering letter and attachments that Richard Clausen asked nae to fax to you. The original well follow in tomorrow's snail. 04oRYMA! A;iVM%A.XANViL FACSTMILE-DoC ffyou do nut recelve this far in its enrirety, or rf arry parr is not legible. please calf (907) 276-2747. 14?11" A 5c � E:u9 Frain -Alaska Anv;l, Inc 90T-279-408& T-767 P 002/014 F-005 ENGIHEERIHG b> SSGN Q�.IQSJ KA 509 YVEW W. AVENWE PPOJECT MANAGEMENT ANVIL ANCHORAGE, AK 986 j-2237 IN$P CTt4N (907) 27Q-2T47 INCflRPaRATED Mr. Jason Wells Valdez Fisheries Box 125 Valdez, AK 99686 May 7, 2003 AL- 1493 Fax_ 907-835-4831 Subic= Conceptual Engineering to Determine Viability of a Cold Storage Facility Using Waste Heat from the PetroStar Valdez Refinery Dear Mr. Wells: Alaska Anvil Inc. has completed the conceptual engineering to determine the feasibility of using waste heat fmm the PetroStar Valdez Refinery to provide the main utility needs of a refrigeration system to cool a potential cold storage facility located adjacent to the refinery. Randy Maag, at Petrostar Valdez Refinery, was contacted and informed us that our originally cnvisioacd high temperature waste heat off the top of the crude heater is already being planned for me by another project. The waste heat he was referring to that is available is the heat from the crude tower overhead vapors that is currently being removed with air fin fan coolers. This is low temperature waste heat at 215 to 2lrF. with a total heat duty currently of 33 MMBTUIhr, when cooled to 105°F. An ammonia absorption refrigeration system is the tape of refrigeration system that would roost jjkqLv be aide to make use of this waste heat and be able to produce the degree of cooling required to attain —20r°F. in a cold storage facility. Ammonia absorption systems typically require a horter temperature heat source than 21 HOF. to achieve the required cold temperature, but due to the relatively cool ambient temperatures in Valdez in the sutmzner, the lower temperature %age heat should be sufficient. Not all of this waste heat will be useable though, only the higher temperature part of it from 218 to about 173°F. which equates to 15.4 NAMBTUIhr. at the current refinery crude rate of 45,000 bpd- The remaining crude tower overhead condenser duty will need to be cooled using the air fin fan coolers. C5-07-03 16.10 From -Alaska Anvil, Inc 507-279-4088 T-707 P 003/Ct4 F-005 Mr. Jason Wells ALASKA ANVIL INCORPORATED Valdez F:sheries Page 2 It is estimated that the refrigeration system will have a Coefficient of Performance (COP) of 0.32. which means that the 15.4 MlvfBT" I/hr of waste heat will equate to 411 tons of refrigeration (TR). Extra care will need to be taken to minimize the temperature losses and squeeze the approach temperatures in the heat exchangers. which means that the size of heat exchangers, and thus cost, will need to increase to accommodate this. .also the only way this is feasible is to take advanuige of the relatively cool ambient temperature in Valdez even in the surnmettime. More than likely there will need to be a coaling water tower to get the most cooling possible for the condensing stage of the anuncinia column. This tower could then be shut down and drained in all but the warmest couple of months in the summer. With these enhancements, it is envisioned that an arnrnonia absorption refrigeration system using waste heat from the Crude tower overhead will produce about 411 TR with an evaporator temperature of —25T. to maintain the cold storage facility at —20T. The rennery was envisioned to operate at 60,000 bpd feed crude rate, which would mean that. if the crude rate increased, there would be an additional 33% of crude tower overhead heat available, which could equate to an additional 33% cooling or as touch as of 1447 TR. The following is an approximation of the freezing and storage process as we envision it, along with the tons of refrigeration (TR) required. Assumptions_, A 45- to 60-day fishing season: 500.000 lb. per day of headed and gutted fish delivered to the freezing plant for freezing and to hold in long term storage. Refinery operation at current rate. Plant arrcas include: 1 Receiving and Blast Freezer Rack Loading Area. 2 Blast Freezer Area (80 % of freezing of product) 3 Holding -Soak Area with "In and Out" (20 % of freeing of product) 4 Long Tenn Storage Area RECEIVING AND BLAST FREEZER[LICK LOADING Temperature: 34T. (Includes storage and rack loading area) Approximate Area-3000 sq. ft. Approximate Refrigeration required =30 TR Production = 30.000 pounds per hour Walls, Floors, hoof R-20 minimum U-9T-93 160 From —Alaska Anvil, Inc 9aT-2?$—d08$ Mr. rason Wells ALASKA ANVIL INCORPORATED Valdez risheries Page 3 BLAST FREEZER AREA r-767 P a04/014 F-005 'temperature: -40 to -50*F. (wheel in and wheel out racks) Approxirnatc Axca-Pcr mf4. design. Approximate Refrigeration Required: 240-300 TR Production - 30,000 pounds per hour. 80-90 % heat removed Waifs: R-45 to 50, Roo R-50 to 60, Floor R-30 to 40 HOLDING/SOAK AREA -ALSO "IN A.N -13 OUT" Temperature: -20 to -25°V {Finish fiecring and transfer from racks to pallets) Approximate Area. = 11, 500 square feet Approximate Refrigeration Required = 80 TR Production = 30,000 pounds per hour. Walls: R-35 to 40, Roof R-45 to 30, Floor R-27 to 32 LONG TERM STORAGE Temperature -20°f . (Pallet Storage) (Area calculated using 33 pounds per cubic foot, 8 toot High files, and 25 percent aisle and open space) Approximate Area = 150,000 square feet Product Storage = approximately 30,00M-00 lb. plus incidentals Refrigeration Required = 300 TR Walls: R-35 to 40, Roof R-45 to 50, FloorR-27 to 32 Refrigeration Required: Long Tcrm+HoldinglSoak-Receiving = 410 TR Blast Freezer - 240 to 300 TR Notes: Daring fish proems-nb times the Holding -Soak: area will require some refrigeration from blast frcezer system to achieve -257. temperature. The blast freezer systein could also be used to provide cooling for the long term storage area and In and Out area during titres when the waste heat is not available. If refinery operation were to increase to 60,000 bpd crude feed rate, the Long Term Storage area could be increased in size to uEflize the additional 136 T'R available. This would trartstate into an additional 68,000 sq, feet of long term storage area for a total storage space of 218,000 sq. feet. 05-07-03 16,10 From -Alaska Anvil. 'nc 90T-i7Q-40BB T-767 P.005/014 F-005 Jason Wells ALASKA ANVIL INCORPORATED Valdez fisheries Page 4 For further assistance, please call Richard Clausen at (907) 677-3099 or Fred Rein. a.[ (907) 677- 3135. Sincerely, yI �. r ...... ...... ...... �..�. i y Richard ClausM P.E. Process Engineering Manager RAC: hkg Enclosures CC: F. G. Weiss 111 5.1Voida rishenesrAC1a93nA'ordConccpwal Engimcring 05-OT-03 1S:I1 From -Alaska Anvd . lot. 9OT-2T9-4088 T-TST P.016I314 F-005 a a nA W r, W � a Q � got, G pEL ea V) 'C] � C p5-{fT-03 16.11 From -Alaska Anil, Inc 907-279-4088 T-767 P 007/014 F-005 ALASKA ANVIL INC. CALCULATION SHEET DESCRIFIION- SY_k�— C—, PAGE_ OrF�'1f yy AIAMI SKA VILJOB NO. �yt3 Cva ��wJ Cac.c��'tcr_ �.�r���'` Crv��Z7 Lk es cd awtm-ontL. sus r�- rci vi Y-mk , . 50 �S 04- nh-L, Izv C70 = 5- Y7 Tk 5'47 —'q M _ } 3 6 T P- a d,.� , � 0 -�i E: From -Alaska Anvii C 9D7-�i6-4O88 T-767 P OOBI914 F-045 Crude Tower Overhead Condenser Curve with crude rate of 45,000 IBPQ feed rate if feed rate increased to 60,000 tapd, the heat flows would increase by 33% Temperature Pressure Meat Flow Enthaipy Vapour Fraction (F) (psig) (8tutbr) (Btullhmale) 218 17.1 0 -64419.86 1 212.4 17 -1805159.35 -55295.31 0.9478 206.8 16.9 -3733214.24 -456230.37 0.8899 201.2 16.8 -5737127.61 -57202.22 0.8281 195.6 16.7 -7778694,95 -68192.33 0.7639 190 MG -9820659-28 -69182.53 0_699 184.4 16.5 -11826353.94 -70155.34 0.6348 178.8 16.4 -13761883 -71094.03 0.5729 173.2 16.3 -15599216.05 -71985.09 0.5147 167.6 16.2 -17318831.49 -72819.06 0.4611 162 16.1 -19356634.49 -73806.86 0.3973 156.4 16 -2225304125 -75212.03 0.3037 150.8 15.9 -24554225.21 -76328.04 02313 145.2 15.8 -26380344.55 -77213.56 0.1762 139.6 15.7 -27844479.2 -T7923.73 0.1349 134 15.6 -29040169.53 -78503.61 0.104 128.4 15.5 -30040083.63 -78988.55 0.0809 122.8 15.4 -30898598.29 -79404.9 0.0636 117.2 15.3 -31655351.61 -7977191 0.0505 111.6 152 -32338706-36 -80103.32 0.0405 106 15.1 -32968726.88 -80408.86 0.0328 RAC 511103 as-or-u3 16:11 From -Alaska Anvil, Inc. 90T-�T9-4089 T-76T P.009/014 t-M ALASKA ANVIL INC. CALCULATION SHEET cuENT DATE G.3 Bra' F61-a7PAGE—Z— OF o�SCRiP>3aN � G rU rasi(A e�rr�it.xl� iva. r�� t4s� P#/ Ly •fir ooCJ /_6 S�Q,r,,lyt7�l7 07-4,L. IML- liV& = 6a4, coo x 60 Doi = .30,ai6,oa64,6 iib�,y i�� 'T fraG13r avo - .9oG9ft-� 645 100EAJ7- Un�rJ 3 3--.3.5- .C6��t3 -- .�otir0 .5rc.Mo - - AFl-j. PR o C- &-5 S f3 L n c It PRO o u c- CI(=-:UC-7-D - 0 2e7J /13� F�o f- FAEF-7z 1A1 6=, F —AI k A I I P 01QID14 C-RAC .[ rom zz a nri nc •'•t•ti'�•,��_�''- IC.�,7�-}����:- _� - .���i� :fit ALASKA AMWL CALCULATION SHEET Cf`I ENT DA t7�5CfiiP31L1N - AL•ASKA AWIL JOB NRAXEihf53 Pp-o f'a s ED /oKo [ -� = � - vr� 1`� p�sCa ��O��,Qp�I�❑� gay _ •[4S20 10 70 1 2. { , 112 S r Z r IcdR__ op6 ' II,J 3ry,Rs pR REMOVG* P Wvob ' I � R>-Rot _�4R3 Ail CE- -5 -Ws ST4 tIa.57g?-m/c6 .cl4X .$=7-15z rA a-6'-33 :6:'2 From -Alaska Anvil, lsr 907-279-409e T-767 P 011/014 F-005 ALASKA ANVIL INC. CALCULATION SHEET CUUJT V 41, j0C ��� 5�1 nArr: a BY 3 AGE; OF p!~SMPTuN &L1J _ �_ ALASKA ANVIL JQ6 HQ-� ---�- _,�_.. 783 5Tu1L0f8 IF7, 920 &7 Z- 4-77171-7J" Hof ov ?C . S �� 2a S� -co-of -- - PULL Dd�►71 `r7rb p �7ro°o .8 r2 f 9-71 MO - -/(7, q � - 2z 5■ LBp -7, 2-o 12- 30� z r �:�- (1.57t - 06-0T-M 16:12 ALASKA ANM . CALCULATION SHEEr CUENT Ul=5CR1Pn0N A) 4. 4 ANVIL J013 NO A. Allow r iV h-►U Q 6 r �T--� — - - lei IS aSe �1�35 IfDf1 ��� :s 1�35 #4k - - -- -- r -- XSul I ' '$ - .. - ._ -tea � •:i-�• ��-- �� � -� C. to► - ��-w ►� s�Y _ ��'o� ©v o �. -.3o ref � .. _ ._._ Frar-Alaska Anvil, Inc OCT-ZTI-4006 T-767 P-01Z1014 F-005 �—+� Osr-OT-R3 3 :12 From -Alaska Anvil, Inc. our-2TH488 T-TOT P.0131014 F-005 r •Lr -�s• _!..4kl'y - .::4 .:: } - • ' ^_ },_r-.; ; • _�'_. - .r-, �+. �,� tea: �+IG�M1�: �: �• a. � • _ r �{: - - e., 7 aLui,6u��t7�i _�! - i •,i_=.i.�; .._�.,; `+mow ANVIL INC. :a. ={y..r : ALASKA r F' y .day_• '�.; CALCULATION SHEET 4 �.- r� = cu arrr4-i.� rsf. DATE o sr aF; 16:`3 From -Alaska Anvil, Inc. 1187-2TI14818 T 707 P 014/014 F-ODE - -- .. --+�,•:�ye..�;.,�il'y '+�:• _�. •qr.'s-'..- •• - -=.:;_ CALCUTA7iGN SHF.ETYY� ?ra CLI rDEISC Ifi PilQl+l 77 � p-r - p OF r� } :m! I u�DC9� ds 0_46 V g#LAfe'ro p�¢.i 7,10 14, -H14 I, J fO 7-0 I I I P-011!p`Jr16 ��-71C "_ _--. .- - - .---� ...-r s.-slur+-as--r. • - . _. _^'!.•-^!:. � •,S It � \ � i Y f .. - - — •• - . �� � . ter:.,,,• _-.-.... ._..