Document 3NKV9oBJ866x5qkQdONXopVg6

ADDENDUM TO THE OPERATING MANUAL CATALYTIC POLYMERIZATION UNIT PLANT 5J TEXACO INC. PUGET SOUND PLANT ESTIMATE 3910 BECHTEL INCORPORATED HOUSTON, TEXAS 1973 WA-TEX 000376 1. GENERAL DESCRIPTION WA-TEX 000377 -5 `X:- I "GENERAL DESCRIPTION A. INTRODUCTION This addendum to the Operating Manual for the Catalytic Polyermization Unit at the Puget Sound Works of TEXACO Inc., Anacortes, Washington, covers the revamp of the Catalytic Polymerization Unit. The principal new equipment for this revamp is: Saturated C3-C4 Amine Treater Saturated C3-C4 Caustic Treater Saturated C3-C4 Regenerated Caustic Treater Saturated C3-C4 Salt Filter Propane Stripper ' Attendant facilities for heat exchange, transfer of liquids, and control of operations. B. BASIS OF DESIGN General In the feed preparation section, the revamp is limited to the cracked C3-C4 treater and the saturated 03-04 treaters. The cracked C3-C4 treaters are to treat 7,963 BPSD of C3-C4 from the Gas Recovery Unit. The saturated C3-C4 treaters are to treat a combined total of 7,017 BPSD of C3-C4 from the Crude Unit and the CRU. : In the recovery section, the revamp covers only the depropanizer. The de propanizer feed Is the effluent from the saturated treaters in the feed preparation section. The condensed depropanizer overhead stream is fed to a new propane stripper from which k20 BPSD of propane product Is recovered. Process flow conditions for the revamped unit are shown on process flow diagrams 5-RA-l and 5-RA-2. - C. DESCRIPTION OF ADDITIONS AND MODIFICATIONS TO THE UNIT This section describes only additions and significant modifications to the Catalytic Polymerization Unit. Reference should be made to-the Operating Manual for the Catalytic Polymerization Unit for a description of the existing facilities. WA-TEX 000378 ( Feed Preparation Section (Reference PS ID's 5-RA-4 and 5-RA-25) The cracked C3-C4 treater3 are'satIsfactory, except, that the 1-inch Raschig rings in the cracked C3-C4 water wash treater, 5J-C5, are replaced with 2-inch Raschig rings. Due to the higher feed rate, the saturated C3-C4 treaters and salt filter are replaced. The existing treaters are left in place, and may be used as standby for the .cracked treaters. The saturated C3-C4 amine treater, C57, has 23 sieve trays. The saturated C3-C4 caustic treater, 5J-C58, and the saturated C3-C4 regenerated caustic treater, 5J-C59, have packed beds of 2-inch carbcn Raschig rings. The saturated feed stream from the CRU and the Crude Unit flows in sequence through the saturated C3-C4 amine treater, 5J-C57, the saturated C3-C4 caustic treater, 5J-C58, the saturated C3-C4 regenerated caustic treater, 5J-C59, and the salt filter, 5J"C60. The treated stream flows through the depropanizer feed-bottoms exchanger, 5J-E57, to the cat. poly, depropan izer, 5J-C17. Tie-ins are made at the amine charge pump, 5J"G6, between the present Amine Regeneration Unit and the new Amine Regeneration Unit (Estimate 3600). The saturated C3-C4 amine treater, 5J-C57, and the cracked C3-C4 amine treater, 5J-C2., may be continued in operation when the present Amine Regeneration Unit is down for turnaround and inspection, by using regenerated amine from the new Amine Regeneration Unit. Recovery Section (Reference P&1D 5-RA-5) The existing depropanizer, 5J-C17, is provided with a new feed-bottoms ex changer, 5J-E51. A new depropanizer feed bypass pump, 5J-G62, is also provided that permits saturated C3-C4 from the feed preparation section to be pumped directly to CRU No. 2. The bottoms product from the depropanizer, 5J-C17, flows through the depropanizer feed-bottoms exchanger, 5J-E57, and the depropanizer bottoms cooler, 5J-E59, to alkylation or storage. The cat. poly, debutanizer, 5J-C19, is not in service, since the Debutanizar in the atmospheric tower overhead section is in service. Liquid overhead product from the depropanizer, 5J-C17, is pumped from the cat. poly, depropanizer accumulator, 5J-C18, to the propane stripper, 5J"C6l. The propane stripper is packed with 30 feet of 1-1/2-inch carbon steel pall rings. Overhead vapor from the propane stripper, 5J-C61, is combined with vapor from the cat. poly, depropanizer accumulator, 5J-C18, and the com bined stream is sent to compressor fuel. Alternately, the propane stripper overhead vapor may be routed through the depropanizer condenser, 5J-E13. Reboil heat is supplied to the propane stripper, 5J~C6l, in_the propane stripper reboiler, 5JE58, by exhaust steam. Propane stripper bottoms prod uct is cooled in the LP6 cooler, 5-J-E18, and sent to storage. WA--TEX 000379 Utl1ities Utility consumption by new or modified equipment Is given n the following table: . Item No. _______________ Service Consumption Exhaust Steam 5J-E58 Propane Stripper Reboiler 585 Lb./Hr. Cooling Water 5J-E59 Depropanizer Bottoms Cooler U6 GPM Electrical 5J-G62 G62A Depropanizer Feed Bypass Pump Spare 7-7 HP i WA-TEX 000380 A^'TV.'vy*1T{ 2. CONTROL FEATURES ! WA-TEX 000381 II- CONTROL FEATURES A. PRINCIPAL CONTROL FEATURES This section describes only additions and signifcant modifications to the Catalytic Polymerization Unit controls. Reference should be made to the Operating Manual for the Catalytic Polymerization Unit for a description of existing controls. Feed Preparation Section (Reference P&I.D 5-RA-25) The control scheme for the new saturated C3-C4 treaters is the same as the control scheme for the existing saturated C3-C4 treaters. A description of the principal control features of the saturated C3-C4 feed preparation section follows. The flow rates of saturated C3-C4 streams from the Crude Unit debutanizer and the Platformer debutanizer are controlled in their respective units. The combined saturated C3"C4 stream flows in sequence through the saturated C3-C4 amine treater, 5J"C57 the saturated C3-C4 caustic treater, 5J-C58, the saturated C3-C4 regenerated caustic treater, 5J-C59, and the saturated C3-C4 salt filter, 5J-C60. The treated stream passes through the depropan izer feed/bottoms exchanger, 5J~E57, to the cat. poly, depropanizer, 5J-C17. The pressure in the saturated C3-C.4 treater section is set by the pressure in the cat. poly depropanizer5J-C17. Control of the cat. poly, depropan izer pressure is described in the following section. The flow rate of regenerated amine to the saturated C3-C4 amine treater, 5J-C57, is controlled by flow controller 5FIC-200. The flow rate of spent amine from the bottom of the saturated C3-C4 amine treater is controlled by interface level controller 5LIC-201 to maintain an amine solution-hydro carbon interface in the top of the amine treater. High and low level alarms, 5LAH-201 and 5LAL-201, are provided for the amine solution-hydrocarbon interface. "Spent caustic is drained ffom the saturated C3-C4 caustic treater, 5J"C58, to spent caustic storage by manual control. The spent caustic is drained when the caustic-hydrocarbon interface appears 5,n level glass 5LG-202. Care must be taken when draining the spent caustic to prevent hydrocarbons entering the spent caustic system. Fresh caustic and dilution water are charged to the saturated C3-C4 caustic treater, 5J-C58, by manual control. Fresh caustic is charged when the caustic-hydrocarbon Interface appears in level glass 5LG-203. The flow rate of regenerated caustic to the saturated C3-C4 regenerated caus tic treater, 5J-C59, is controlled by flow controller 5FIC-201. The flow I WA-TEX 000382 { rate of spent caustic from the bottom of the saturated C3-C4 regenerated caustic treater is controlled-by interface level controller, 5LIC-205, to maintain a caustic-hydrocarbon interface in the top of the regenerated caustic treater. High and low level alarms,<5LAH-205and'5LAL-205, are provided for the caustic-hydrocarbon interface. Water that accumulates In the bottom of the saturated C3-C4. salt filter is drained to the oily water sewer by manual control. The water-hydrocarbon interface may be observed In level glass:LG-506. Recovery Section (ReferencePSlp. 5-RA-5)>.; ' The amount of saturated 03-04 from the fped preparation section that is pumped directly to CRU No. 2 is-control |ed by-flow controller 5F1C-205. When the propane stripper,-5J-C61, is ln>operation, a vapor product will be leaving the depropanizer-propane strapper-system. For this case, 5HCV-6 and 5HC-20 should.be positioned spch that the depropanizer pressure controller, 5PIC-106, positionsfpontrol valve 5PIC-106VB to adjust vapor flow from the system, and the cat. poly.\depropanizer accumulator level controller, 5LIC-b9, positions control yalve 5PIC-106VA to regulate cooling water flow to the depropanizer condenser!, 5J-E13. Feed to the propane stripper will be regulated by flow controller 5FIC-207. When the propane stripper, 5J-C61, is not in qperation, an all liquid cat. poly, depropanizer overhead product may be obtained.- For this case, 5HCV-6 should be positioned such that th$, depropan iz.er pressure controller, 5P1C-106, positions control valve 5PiC-iVA to adjust cooling water flow to the depropanizer condenser, 5J-E13, ahd ther cat. poly, depropanizer accumulator level controller, 5LIC-49* rdsets the net product flow con troller, 5FIC-207. Noncondensibles may be vented from the system peri odically by operating hand controller 5Hfc-20 to open,control valve 5PIC-106VB in the accumulator vapor line. ^ description pf other controls on the cat. poly, depropanizer is given on ppge 21 o;f the Operating Manual for the Catalytic Polymerization Unit. ). The temperature of the propane stripper feottoms is controlled by temperature controller 5TIC-205 that adjusts" condensate discharge from the propane stripper reboiler, 5J-E58. Level in the'bottom of the propane stripper, 5J-C61, Is controlled by level controller 5L!C-;210 that adjusts discharge of LPG from the stripper. V i WA-TEX 000383 3. PREPARATION FOR STARTUP WA-TEX 000384 Ht - PREPARATIONS FOR OPERATIONS Reference' should be made to the Operating Manual for the Catalytic Polymeriza tlon Unit for a description of preparations for operations. ' WA-TEX 000385 ( if. STARTUP PROCEDURE WA-TEX 000386 < IV - STARTUP PROCEDURE A. GENERAL Reference should be made to the Operating Manual for the Catalytic Polymer ization Unit for a description of the startup procedure for existing equip ment. The startup procedure for the new saturated C3-C4 treating section Is similar to the startup procedure for the existing saturated C3-C4. treat ing section, and the existing procedure should be used. B. RECOVERY SECTION ' The cat. poly, depropanizer, 5J-C17, and its related equipment, can be started up by the procedure given in the Operating Manual for the Catalytic Polymerization Unit. The new depropanizer bottoms cooler, 5J-E59, and the new depropanizer feed/bottoms exchanger, 5J-E57, are steam purged, tightnesstested, filled with fuel gas, and brought onstream in conjunction with the cat. poly, depropanizer. The following procedure for startup of the propane stripper, 5J-C61, and its related equipment, assumes that the cat. poly, depropanizer system is oper ating. The same procedure, with minor modifications, can be used for start up of the propane stripper in conjunction with startup of the cat. poly, depropanizer. An outline of the startup procedure-is as follows: 1. Steam-purge for elimination of a;i r. 2. Tightness-test and gas-fill. 3.. Inventory and circulate to dry. 4. Adjust operating conditions. Introduce steam through the steamout connection of the propane stripper and vent steam and air through the 2-inch vent at the top of the propane stripper. Permit the tubes of the propane stripper reboiler, 5J-E58, to fill with steam condensate. When the propane stripper is thoroughly purged, as evidenced by a strong show of .steam from the vent, throttle the vent. Purge the propane stripper overhead line,-. SJ^O-ZIS^", to the block'valve at line 6,,-5J"0-45. Purge line 5J"0-220-3" to the.block valve at line 4"-5J"0-l62. NOTE: The propane stripper feed line, 5J"0-225_3", and the propane stripper bottoms line, 5J-0-224-3'*, have been purged and placed in service. These lines will contain hydrocarbons up to the block valves at the propane stripper when the cat. poly, depropanizer is in service. WA-TEX 000387 ( Close the vent valve on the propane stripper and tightness-test at 25 psig with steam. Drain steam condensate from all low point drains. After a successful tightness test, reduce the steam pressure to about 5 psig. Slowly pressurize the propane stripper by allowing cat. poly, depropanizer overhead vapors to enter the propane stripper through line 5*1-0-219-3". Drain steam condensate from all low point drains. Inventory the propane stripper with liquid from the cat. poly, depropanizer accumulator, 5J-C18, through the propane stripper feed line. Commission the propane stripper reboiler, 5J~E58, and allow overhead vapor from the propane stripper to pass through the depropanizer condenser, 5J-E13, to the cat. poly, depro panizer accumulator, 5J"Cl8. Add inventory to the propane stripper as re quired. Continue operation in this manner until the propane stripper is free of water. During the above propane stripper drying procedure, 5HCV-6 has been posi tioned such that the cat. poly, depropanizer pressure controller, 5PIC-106, regulates cooling water flow to the depropanizer condenser, and the cat. poly, depropanizer accumulator level controller, 5L1C-49, resets the net overhead product flow controller, 5F1C-207. The net liquid product passes through the LPG cooler, 5J-C20, to the chiller. After the propane stripper is dried, it may be brought onstream by the following steps: 1. Reroute propane stripper overhead vapor from the depropanizer condenser to the cat. poly, depropanizer accumulator vapor line, V-5J-0-162. 2. Reposition 5HCV-6 such that the cat. poly, depropanizer pres sure controller, 5PIC-106, regulates vapor flow from the cat. poly, depropanizer accumulator, and the cat. poly, depropan izer accumulator level controller, 5LIC-49, regulates cooling water flow to the depropanizer condenser, 5J-E13- Flow of net liquid from the cat. poly,, depropanizer accumulator is regu lated by flow controller 5.FIC-207. 3. Net liquid product from the cat. poly, depropanizer accumulator is rerouted from the LPG cooler, 5*1"E18, to the propane stripper. k. bottoms product from the propane stripper is routed through the LPG cooler to the chiller. The propane stripper level controller, 5LIC-210, is put in service to regulate flow of propane stripper bottoms. . 5. The propane stripper temperature controller, 5TIC-205, is put in service to regulate steam condensate flow from the propane stripper reboiler, 5*J~E58. ,, I WA-TEX 000388 * t; v ' .. SHUTDOWN PROCEDURE WA-TEX 000389 VI - SHUTDOWN PROCEDURES Reference should be made to the Operating Manual for the Catalytic Polymeriza tion Unit for a description of shutdown procedures for existing equipment. The shutdown procedure for the new saturated C3-C4 treating section is similar to the shutdown procedure for the existing saturated C3-C4 treating section, and the existing procedure should be used. The propane stripper, 5J"C6l, is shut down in conjunction with the cat. poly, depropanizer, 5J-C17. as follows: ' 1. Discontinue steam to the propane stripper reboiler, 5J-E58. 2. Pump out liquid products to storage as described in the Operating Manual for the Catalytic Polymerization Unit. 3. Depressure the system to flare. k. Purge the system with steam to remove all hydrocarbon vapors and vent to the atmosphere. Emergency shutdown procedures described in the Operating Manual for the Catalytic Polymerization U.nit are applicable to the new saturated" C3-C4 treating section and the propane stripper. WA-TEX 000390 ( 9. SAFETY FEATURES s REGULATIONS WA-TEX 000391 IX - SAFETY FEATURES AND REGULATIONS Reference should be made to the Operating Manual for the Catalytic Polymerization Unit for a discussion of safety features and regulations. The new relief valves installed are listed below: Relief Valve No. Service 5PSV-101 Saturated C3-.C4 Amine Treater, 5J-C57 5PSV-102 Saturated C3-C4 Caustic Treater', 5J"C58 5PSV-103 Saturated C3-C4 Regenerated Caustic Treater, 5J-C59 5PSV-10i Saturated C3-C4 Salt Filter, 5J-C60 5PSV-105 Propane Stripper, 5J-G61 All of the new relief valves discharge through the existing header system to the existing blowdown drum, 5J-C29. Bypass valves are provided around each of the new relief valves, so that the related equipment can be vented to the existing header system. f WA-TEX 000392 - .<' ( .10 appendix WA-TEX 000393 ( 10.1 PROCESS AND UTILITY DIAGRAMS - l \ WA-TEX 000394 ( PROCESS FLOW DIAGRAM 5-RA-l WA-TEX 000395 I PROCESS FLOW 01 AGRAM 5-RA-2 ; WA-TEX 000396 f^iura _ y&ia * tfcl 0E5IGWAU0M. ilfrf.tcicaw>nt.) . _ t 0CUTfLu?o0* SVMfrgLG TEJCACP t*>T. 99IP ----------- - t * * A'-6- 6 o-co-9 ^ et!4TlN<> N8W fttUpvft e.l0cA1t ucr u&eo-pp mpt slempvs OSWpTIf T>t*m WUMftfiR* /K Mgrgft I, 2fcV-M<?NS Of UiJOG. 6Vf.rf.l4* Afc 6>l6NATEt> <w TV6 *ymc*.s swoww AScwe. M>pa- ( R.tvi*tPNP A<tfe oftc-utp Awp.iucuo&fc & TfcAN6ULAJU REVJ5IPW MARt. f; ptPiHt, ^Ecvitie specification* tott mew uwe Aftt IN *A*iO#DA>lCt WltH <hEM* J'70d . TAfcut T, . $, uwt VJ(9 *0PPt*t* Poe, IW4.Ul.MioN ON NEW - *. t.IM. PPOfdMMCMpSTCCcTpCl AM. PPO4UCpEATUPPOOt8&LEtELTL4ARU?MlPf4A>UUMTAUUEWlUCFAMTlOElMTLCAOUNEOTtACA>$*TCiOCPtEAE*NRRIPAMSOv0PACNtfTceTCE6OaI1VC..NLOAATSLTTNvIOuOUMI.OtVNRAU*TO*E;MCPONT>.ROL, ll mSfttoyou MAttPMC E LINE IDENTIFICATION `J'C 18-4--JIJA-HI . ,f f *---------MJUtATION m* km SIZE .. | *EQUIXCMENf$ LfCXACO PIPING MATERIAL ^HUMUX sttVlCfc SPECIFICATION yv ybA **-* i 4 P_____ A * * (. * UU fc- 5>oiri r>B| &I,T; jj -. t Stouutr. |5*0ll fe * :" ' V dr *>**<* 'k 1 ' ' /-. $ I mm 4- Pit A t-t-7S REVISED JkAAMCI PER DRAWING rey.o 4* r<k. Pp Aopera ujilrry SWPoiii#.*<3 f3C % ST-ST-l5*lh*Jfti-PM& V 2 SIMUAP POt CONSTRUCTION - fa %A UPWTE& 7 *400 AWMD IWUtP K>8 APPRCVlL . . ne .Mb ** ft eu Si i* a ** MALI | SOUWft MUM , BF.OHTEL 1E&AGQ iHO. PUOCT tOUMD fLANT mm. UTILITY PIPINGS INSTRUMENT DIAGRAM STEAM i CONDENSATE SYSTEMS CATALYTIC POLYMERIZATION UNIT A*)Mk *t*m- lam nxAccm- Pi 5-AA-7 w. flA WA-TEX 000397 t s r*i -c 5. H* -6 H IHAHfysaB ^ I n 3* WA-TEX 000398 ntAHou RATION WC. ,0iit wuwftEQ {.iiavici otimAnw true <T.f.o.) ;t/MSfoCMCUIEi} ti ' . WON >ou,ruEucfl.s It nou ,->& * , u*> st-e-nt * juA V'-SJ'-P-TPO 7l,vl">`-/ Ncrv Y*\y*V*\ REMOVE -6~&- &-- RELOCATE O -O O 1 MOT OSCO (00 MOT ftfMOVf; demotes re*w numbers { I jj MOTES t REVISIONS OP MAJOR SYSTeMS Aft DESIGNATED tfY THE SYMOOLS SH0WK ABOVE. MINOR REVISIONS ARE CIRCLED AMD INCLUDE A TRIANGULAR Revision mark. t,, PIPING SERVICE. SPECIFICATIONS TOR N6W LINgS ARE IN ACCORDANCE WITH GEMS J-RCB,tAeU 7. $ LINE NUMfcfR SUPUXES FOR tVt$lKAT>N ARE IDENTIFIED AS FOLLOWS* PP PERSONNEL PROTECTION CC Cctf> CONSERVATION PMC PARTIAL HEAT CONSERVATION FMC FVU HEAT CONSERVATION OTC OPERATING TEMPCRATURe COHT&OL ST STEAM TRACED Nl MO INSULATION LINE IDENflFICATfoFT ........... J-V-J13A-HI jth ? f t---------insulation SIXC I RIOUISEMINTS HJmk. ftss J TEXACO PIPING MATERIAL LnumBU SERVICE SPECIFICATION . a yfcK *--4 i f VTION |fANr <f> < 0U69AM --1 jTSuy.s >uv W H* AA-IO X ft Z-t-7S AV6AVAI&*UBOO PRfePR.V.lRAAV/lNO A Hr RSt-VAlAS-EJOIOPERREDVR.OAWING bp '*c it r<^- A %. %, io*vfO ft?*. cov$m>citcn UISPSOU*aEeDd>PToOe AJcPfcP*RCD*tVJAiLAS> 74 v >T $Cm* jte Ufi K. w 'isni home '( __,_ 1mw BECHTEL HOUSTON TIKMFiHfiT U6tf SOUND HAN! UTlL/TY PJPMGt IHSTflUMEMT DIAGRAM A/ft i SLOWDOWN SYSTEMS CAT. POLY. UNIT Mk. titXTU- 1* nutfriR* 3*9 0 T<< to1 **** ilA WA-TEX 000399 1* Hilt VVUU ' n:`44 *0 . >:5 I 1 t I j` ..: j ------- ----4 h eiCrtTU-10095 SYMBOLS TEXACO E5C-39W ---------------- -i* */ r'- .fH-o-fr-- EXISTING NEW RCM<7/f RE10CNTE NOT USED COO MOT REMOVE) DEMOTES TIE-IN NUMBERS Motes . REVISIONS OF MA/OR SYSTEMS ARE DESIGNATED 8T THE SYM0CCS SMOWW A&$V& MINOR ftfiVl55NS Ag CIRCLED AND INCLUDE A TftlAH&ULAR REVISION MARK. i PIPING SERVICE SPECIFICATIONS fO* NEW LINES ARC W ACCORDANCE WITH GEMS ^Dfi, TABLE ?. a LINE NJNibEP SUFFIXES FOR INSUIATIOHCN NEW AE JOEPTIFieo AS FOLLOWS: ` PP PERSONNEL PRO TfiCf3N cc COID CONSERVATION PilC PARTIAL HEAT eeHSSRVAriOM PNC. PUI.I HtAT CONSERVATION OTC OPERATING. TEMPERATURE CC TROL ST STEAM TRACED . Ml MS WSUlATtOM - .A ffisMsS Stlit fI - t,------- IBNfSOUULHAlITMIOENNTS &A& &L j ttXACO PILING MATERIAL LNUMKR SERVICE STECItlCAItON r- i*QAi 2 ( v.*TT| S.IU'O 1 'Vii*"io J >1-34*1 1 1 SAAft 1 ijrt-t 1 <--v~ hi la*M v '* ` M, "BE6HTEL HOUSTON 63 HIOET SOUH& FLAKY UTILITY PIPING k INSTRUMENT DIAGRAM WATER SYSTEM CATALYTIC POLYMEfMZATfOtf tfKIT [kiwu> mom [toutim- J*W . --------- 5-AA-ll pfij wa-tex 000400 ff : REMOVE RELOCATE * -- NOT wSEO COp NOT REMOVE) denotes Ti-m numbers MOTES Revisions of major systems me OCS!rWATCO 2t THE SVM&OtS SHCWH AMV. MINOR AS\6N& ARE CIRCLED ww<.AND iNCLt/OE A TRIANGULA* REVISION P|PJN& SERVICE SPEC*FtCATIONS FOR HE/* UNES ARE *U ACCORDANT WITH GEMS J.2C4 TABlB?. LINE NUMOER SUFftKES FOR iN.SULATtCkt ARC IDENTIFIED AS FOLLOWS, PP PERSONNEL PROTECTION COLD CONSERVATION PARTIAL NEAT CONSERVATION FUU NEAT CONSERVATION OPERATING TEMPERATURE COMTCi_ STEAM TRACED NO IM5ULAT(OM 70 RELIEF HEADER 'A! ^Y-IOSUS : ( ^W*STCl*Jrt*'ST -- LOMtBQL VALVE (UOt OU Aift --%-- $ncuut taiviD O^M&r OHAU '> AUfct* couiaoi XAIYI muurw* jtuw T**etO pp.^wcwwtt monatox SPtClAClfc SltMO H4T m&TBUMEMT SYMBOLS tUP MOWMTID 60X00 HOUMfED ms*. uueCMrtc. ccm iWAKHUOMJftOl xiauue juVuv tH{ljAt VMQ cxmuoytyMHoJ -PiAur uuhmb /JAIN--lUMBUMtMr lOEWNUCAUOU \jb/--iwwftoneNT uoMfctp ail iurngHlUtwSTr6ttUAMRfEtcMoeTepiMIPEaiMcoToI CdalfucAciTtvOmAim# i.va, STANOAftD* IXCCP? AS MOtIDUK* UAY MU* TO 0*6*JO`IA- UU5 IP6MT1FICATI0M TOft UN*V WHtftt VilOClUfr Au 0811VUM CRO& HIM tt UUUUTI* OiPiw* APlc,-* S7ft----- --* 111 r-UMl MOIAl vt AC. PU*)TW*- [ A---- COHHOOttY Kt immVA*o tnaum *ot atouiemct m*--c**t"m- oT.pT.c<ho.cMuuAtNi*ovx*: - ............. .... PILING WttIPItMIW Jtw-M6 IOO-W0M. 76" coax. AU0Y6 1 , REtOCATE HOT USED COO HOT ftMOVC> DENOTES TIE-IN UM*P& MOTES j I. REVISIONS or MAJOR SYSTEMS ARE DESIGNATED BY THE SYMBOLS SHOWN ABOVE. MINOR REVISIONS ARE CIRCLED AND INCLUDE A TRIANGULAR REVISION MARK. |2..PIPM& SERVICE SPECIFICATIONS FOR NOV LINES ARE )N ACCORDANCE WITH &EMS J-0* TABLE 7. 3. LINE NUMBER SOFflKES FOR INSULA.TMM ARE IDENTIFIED AS FOLLOWS* PP PERSONNEL PROTECTION CC COLD CONSERVATION PHC PARTW. HEAT CONSERVATION *y<r FHC FULL HEAT CONSERVATION a&> OTC OPERATING TEMPERATORC CONTROL ST STEAM TRACED , . H NO INSULATION = / 4.70 Keep WIOZOCbtLbCH' FZCH tHTtClHG SUAH ' CONPtNSATK GYS7SM. THfi BALL PU?M GHRLL ftft SET 70 SHUT OFF FOC UOlD OF SPCWPI& GaXVlTV LESS TN6H WATER. ^S*i,W^fAa+Jr 6rAM1ftAC*^ JSVMBOUS* , Gk Bi-TBAce& .* Q5ftTeased j mousbo , ^ --. LINE IDENTIFICATION i A - o-;,?- &-h?a- *. |T I t --H?C*#IOW t V*ukaco. 1 x.l U AOLIjuurol site m>TMTOLlKlrMe9 l| YS{C>KAV`.l<CJtFSVlwSViM CMAMHCORNiAl a /V JO* JIB )SOt<L GAIE?T55&* COflB, Allow t0* COCKS, !A0' CCftft. AUOW. JO.fclS JO.&SS ;o.o? 6ATE4, `Aa- COilR.MlGVL SOO*R.F. COCKS.Vio*COW. ALLOW. 50* *.F. COCKS.//,e* C0<ur.^tt0W. <iya*-s < 4? i-QA?> :t-two-nn--->n-cX -S3E^ COMMODITY Ct SI SkiAT| OH <{MDtH)in IWUR KTCACCAMWUiQgJB PA wri run $n { sas stum (cummin ITEM NUMBERS 7rnco..(^..ot mw far*.* Wm.p.c.*., nuo um `ackt. HEFtRtMCS OR AY# I MG & Moci55 o&i.p.- rteo mAstci. ext. poiy. vmt oaoctss frM.p^fcmToA-ucrw.povY. wrr _____ UUVltV~RL t D.-.MCAM & CWPWWlt' SVSttMS omniunrtvy . &p.ci.o> water systems poi o mh slowdown oyojems P6T.t).-TAUKA0t tlMUntCMWlCTIMO PlOT PtMi-CATAlYT/C WlYMIRIJATlOU UNIT HJ*3AA*.>' A eu oor MOTES I. . TftlON*Of vissittnn tol mAccOAMHCt WJJ* Deft..tt'Al'()) U MB*,UmoDi tlYlH Ue' 0*1 er>*tt 4 pfy- AOO.5* PAR' twx. sj*cii & ?Ilf* *{*&wr.AvIiMiw# p5*U-IP? A iitllUpTnIfPt.* #f rfAAVa5nfl t VTVM utt q# xty. m put, l-u^n-i A^ frrUu>> Fgvmop>t< tn IW.ttA;ltl i rotnjsrorqeV'OExt^^cZcirr JA s fejaya^'agBsr A >-2t>51 t45mt> Cf>a APPftOVAV MOO--JL H6vt #r _&22L BECHTE1 .CORPORATIOM , 5AN KANCISCO IHi TEXAS COMPANY fVCZT SOUND WORKS PROCESS PtPlfJG S IM&rnOM&MT DIAGRAM nicoveev Geertoo CATAtYIK POtYMtQttAHOM UM'T 2525 WWK% _____~j " Hi ts K AOMSoNSfSi^H33T,^BTE3WT^_ } -nUAvv* CYMGCX-S AS NOTED >) Apput> LIflu' 3 OTiVOTV 7IU-JM U3-U*-LT-Cfc`o -VMua.tOBtf Pttft _ RRV. ' rfe \aMjKeafeh-g .1 5SJ I REVISED PER ORAWIMG Tt r ^^jls^A-iqS ^REV^O ________ {%] ISSUED TQfl. CONSTgUcribU m[ ISSUED , "____ :>lt NOME I ClFWftO BEGHTEL TEXACO IHC. FUOIT SOUND PLANT PROCESS PIPING INST. DIAGRAM RECOVERY SECTION ' CATALYTIC POLMERIZATIQN UNIT nr worm- tCOM RttHIR. 9*>9 r--' 5-RA-5 H8A LITY LEGEND R - OILY WATER STEAM ?- SERVICE I I NOTES. SUFFIXES FOR INSULATION T> AS FOLLOWS: WIEL protection CONSERVATION AL HEAT CONSERVATION HEAT CONSERVATION TING TEMPERATURE CONTROL I TRACED a INSULATED 1ULATION (WISE SPECIFIED. THE VALVE ALL BE BY THE CONTRACTOR is J-ID, PARA.513 FOR' '.OSOPHY WITH REGARDS BE SUPPLIED BY THE 'ARTICULAR .ATTENTION EN TO THE MODIFICATION WHICH COVERS SHUTDOWN r-FOR &ECMT&L - ICC95 T6XACO E5T. 3910 tr 0 5VM&<?L5 EXISTING NEW REMDVE RELOCATE NOT USED-DO NOT REMOVE DENOTES TIE-(VI NUMBERS Notes Zlk I, REVIO'CN OP MAJOR SYSTEMS ARE DESIGNATED &Y THE SYM&dlS 5MOWW ABOVE. MINOR PEVI510HS ARE CIRCLED AND INCLUDE A TRIANGULAR REVISION MARX, ' 2. piping seavice specifications for new LINES ARE IN ACCCRoAUCE WITH 66MS J-'ZDB, TABLE T. 3. LINE NUM6ER SUFFIXES FOR. INSULATION ARE IDENTIFIED AS FOLLOWS? PP PERSONNEL PROTECTION . cc COLD CONSERVATION PHC PARTIAL HEAT CONSERVATION FHC FULL HEAT CONSERVATION OTC OPERATING TEMPERATURE CONTROL ST STEAM TRACtO ' VNt JiO lfi^ULATlON__ 4 STtiv TRLNOiKCt sy \ujo_s : a- ta^.*d 7\ ^ ?ThI- Tga.CSOT LINE IDENTIFICATION IAA-00--1133P?--66 --JJT133AA- Nl r r. 'r *1 T* TEXACOJ TEXACO I SIZE * -------INSULATION REQUIREMENTS PIANT NUMBER! SERVICE I SYMBOL LNhuUmMbBeE1R, |L_ T< EXACO SERVICE PIPING MATERIAL SPECIFICATION 0 4: jiijoHWiNto A*r the rwonnn ninco OIMRWItt \CO INC. 1G DEPARTMENT TON. TEXAS 46 FLOW DIAGRAM ARATIOH SECTION 'MERIZATION UNIT . NONE lit A9*I0HR> no xcoro trnnu OAT* 1 - 21 -72 5-RA-25 Serf*1 it.-v sco~LPJi,7;.o si-CLi-------------- AOSSS5 N.sr^cvtefsT ST?A.N\ -c. j * ' TftOC'^C. S.YW2>LS At S5TC3> %;} 4 \Vfy ADD5D FL.&S TO -CPUIE 3J-0-R-PO $ p<EU2TlfU ST' FFPr-1 ,0.-C-a.X. 7>\Zi (Levilcd pur. .S.:A A^os...&E-v^la- REVISED PER DRAWING 5-AA-I25 REV.O Vo icvta2k ISSUEO 'OR CONSTRUCTION KMH T>1J maW IMiltB ftttlWXL & e%i- & VA Tj>tJT VJ4 SCALE HCNS I BtSHUItn BECHTEL TEXACO INC. PUGET SOUND PLANT PROCESS PIPING S INSTRUMENT DIAGRAM ^.SAT FEED PREPARATION SECTION CATALYTIC POLYMERIZATION UNI" & BCCHICL- t0095 USAtOWt- 3910 5-RA-25 7A WA-TEX 000403 I & ( 10.2 VESSEL DRAWINGS WA-TEX 000404 ( DRAWING 5-DC-40 ; WA-TEX 000405 DRAWING 5-DC-Al W&-TEX 000406 1 DRAWING 5-DC-42 { WA-TEX 000407 DRAWING 5-DC-M ? WA-TEX 000408 t DRAWING 5-DC-44 -M wf WA-TEX 000409 10.3 EXCHANGERS WA-TEX 000410 . `. ' / .^V >-v i- '' >".''v - ,, .. ^ ^ - ,, ... . a :- ;i *. ':i =>: ...% (. r '%.'*** ;... %?- ;^r . y;:!;4 '-.V; . i--. ;. ' r& *A.<-jL.v "=. -yV. V { Vvv- ,`y^-. .- j.-; . - > t. . .f.vV- V -;: ->' : :i: y Vi, .. * V . **: u~ * fe MiJi % .'**' ' ~table iq.3-1:- >' ?; ;>& r^v-;. ^ SUHMAF m )AJA , ^. :r" ' ` t /V '- tv . \v.* tr :-r . .V, DESIGN >.T: .* - V.; * Shell Oata Shell Tube No* Biam. No." Temp Press Temp Press 1 Passes Inches Ha terlal Passes PSIG PSIG t 2 2 i. 6 15~1 A 12 19-1A c.s. c.s. c.s. 1 , 650 I 400 1 650 300 650 65 200 300 300 300 275 150 >: 7 ; ?'; , ^ - . v' _ V/ . >.. bVv'v -v . ^ y,-'.*' * ;. v v , -v' v . . v _. - - 5 ; . ' ' ' :;*? VV *" : ;>V: , -7 - . r ' ; *. . !-; . , :< ' V -W. 1;' ; - I. '. .fi -I'"'.'* , <" !. :V ? -'i:>S r- .' ` .? 4 .. *' * 'V r* \ v ' ' * *. :: v. - * V. . O. ' r%i ' . * ' ' '. =' .' . ", X' 'si/WV. rij- :* '-.r. . -v iJ**H'* -*`s ^ fc,; . ` ' ;l'v kv^* 'C v 'rj;-,' ; - fa-TEX 000411 ^ ' . . ' =>' . " Vi v .--.'-f. .4 > // l EXCHANGER SPECIFICATION SHEET 1 CUSTOMER AND 1 R PROJECT LOCATION Tk'SAA.C.O \*4C______ ___ ]l j PLANT *" j , exchanger no. 4 . 1 SERVICE OF UNIT Poc,BT SoUNO ST- C&& ...... PfioPKNC St0.1F>. 5 size |1k72 TYPE 4CO CONNECTED 6 SURFACE PER UNIT 3g EFF. +U. SHELLS PER UNIT | IN EXCHANGER MFR. ttubULS -- KhoCRSON REO. NO. fe-2. ITEM NO SERIES SURFACE PER SHELL QS parallel FF P PERFORMANCE OF ONE UNIT 1 FLUID CIRCULATED 8 < TOTAL FLUID ENTERING 91 VAPOR LBStoft SHELL SIDE Steam 5&S . TUBE SIDE PropawMG. Stripper Btm S<bOO 10 9 11 i LIQUID steam 5&S. ... 9<bOO 12 1 NON-CONDENSIBLES 13 | FLUID VAPORIZED R- SONOENS 14 ] STEAM CONOENSED 5&5 IS 5 GRAVITY-LIQUID 16 j VISCOSITY-LIQUID C.p O. 4-4p 0.003 t\ui - O.OS /Oot) 17 J MOLECULAR WEIGHT-VAPORS 4- 3.a 18 ( SPECIFIC-HEAt-LIQUIDS B.T ../<* BTI|/f 19 ,1 LATENT HEAT -VAPORS 8. T.U./W 8TU/# 20 fj TEMPERATURE IN 21 A TEMPERATURE out 22 j OPERATING PRESSURE PSI 23 NUMBER OF PASSES n \ VELOCITY _i | PRESSURE DROP allow/calc. 26 ] FOULING RESISTANCE MIN. 27 22. 1 251 35......... 1 l.o / e> 0.0005 *F *F ft. /sec. * /SO.IN. ........ W'l life ______ 235 2 0.5 / 0.5 0.001 *F *r FT /sec P/so IN. 26 j HEAT EXCHANGED-BT.U./HR 29 TRANSFER RATE- SERVICE 540.000 35 CLEAN M T.D. {CORRECTED) |<o2 ACTUAL FOULING FACTOR 30 | DESIGN PRESSURE 3) [ TEST PRESSURE 32 DESIGN TEMPERATURE o33 tubes Carbon firttu no. 34 shell Cm%Bom Steel CONSTRUCT ! C N G>5 too */0.IN. */M.N. 400 r o. d. 04oOp&53m 27length 1. 0. 12" . THICKWESS 275 4*1 S 200 PITCH 1" jf/so in */$Q IN A 35 -SH tLL COVER CABBoN StIEL. floatmic HEAD COVER . 36 . CHAN.NEL CAkgftoU `oTtt.L |37 tube sheets - stationary Cabakm CHANNEL cover CAKBom 5tcku .floating 38 BAFFLES - CROSS CA.E2rn.nwl Grftl TYPE Sec. KCWTAvU THICKNESS 39 j 40 j 41 BAFFLE - LONG ' TYPE TUBE SUPPORTS Mmn.GASKETS_____ Tackctep Aabcstos_____ THICKNESS THICKNESS 42 I 43 j 44 i 45 46 CONNECTIONS-SHELL- IN 2" -CHANNEL-IN 3" CORROSION ALLOWANCE --SHELL SIDE OUT _O_U_T. __ \* 1" 3k* RATING ISO*RF RATIN6 300 otr* TUtE SIDE CODE REQUIREMENTS A4HC SRCTlOKl Vl Dl TEMA CLASS ____R WEIGHTS - EACH SHELL BUNDLE FULL Of WATCH spec. ' tM7 . 47 NOTE INOICATE AFTER EACH PART WHETHER STRESS RELIEVED tS.R.l AHD WHETHER RADIOGRAPHED t X-R> 48 REMARKS - - . _y_S\ 9t ' . m A OAT A B5.yiSgE> A *2S 1SGUS.O Ra PUKCHASt TV* JOB' NO. DRWG. HO. I REV. * *ioo^$ OS-Jferfc-3 I LU WA-TEX 000412 FORM H. 158 PART B 9 /6 5 l EXCHANGER SPECIFICATION SHEET | CUSTOMER AND R PROJECT LOCATION XEX*CgJ}!ifei.-- exchanger MH. WtfcTBEfAH So*WV___ I PLANT 'S EXCHANGER NO. PoctT Sound, $7 51 REO. NO. 6^-03_____________________ ITEM NO SERVICE OF U.MT DEPBOPKHmRFEgP BOTTOM EXCHANGER ... SIZE jS___K____ZAO__________ TYPE AsE.S_________________CONNECTED INSERIES parallel 4-73SURFACE PER UNIT EFF. SHELLS PER UNIT 4-73SURFACE PER SHELL EFF PE R F O R M A N C E OF ONE UNIT 7 I fluid circulated 8 * TOTAL fluid ENTERING 9J VAPOR SHELL SIDE OKjPROP>ikHitz.f:tt. (TkcD LM/i BS-357 TUBE SIDE Oc.propaNI2e.r Btms. A<z;ZS7 10 1 LIQUID 56,3S7 4-3 v 767 _ 11 1 STEAM 12 M NON-CON 0ENS1BLES 13 H FLUID VAPORIZED OR CONOENSED 14 i] STEAM CONDENSED 15 [j GRAVITY-LIOUID 16 H VISCOSITY -LIQUID 17 [] MOlfCULAR WEIGHT-TIROBRt Cp O. 54 C Iki') - 0.4-94* COot) O. 14 (In) ~ 0*1 (Out) 55.& 6"4S9('Hy- 0.514 (out) O.OSS.(lM>-O.U (Out) 567 specific heat-liouids i* latent heat -VAPORS 8. T .U./W 8. T. U /W 8IU/F BTU/4 ri temperature in ft TEMPERATURE out 1} operating pressure PSIO loo.................. *F 1&4 *f 745 216 15423S *f *f NUMBER of PASSES 1 VELOCITY ll PRESSURE DROP 3 FOULING RESISTANCE ALLOw/cALC. MIN. I 5^2 0.001 ft. /sec. * /so.in. 1.5 2 4/ 1.5 0.001 ft. /sec . /so.in H heat exchanges- btu./hr j TRANSFER RATE- SERVICE 1 S DESIGN PRESSURE [ TEST PRESSURE OESIGN TEMPERATURE 1,650.000 m t.d. icorrected) 4Qs 9 CLEAN CONSTRUCTION ACTUAL FOULINC- FACTOR 300 */so.in. loo o/sam 4,5 o w/so. in. 450 w/so m . ____________ fe5<_____________ --_________ ___________ ase________ ________ if_________ SHELL CAsRBOM Stckl SEEE C0VE* carbon Steel :f'HflNNEL Ca.rk.oki Steel iy.SE.SHEETS - STATIONARY CARBON P. IS STItL______________ THICKNESS FLOATING HEAP COVER CARROM &TEEL CHARNEL COVER CKXUIt*r>W t- FLOATING CAR&OH StCRU.. _-_CROSS CABQKt StKEL type S.C.MHTA>UhickrEss .BAFFLE - LONG TYPE' THICKNESS TUBE SUPPORTS THICKNESS GASKETS MSJAiW JAcKETEO AfrftftgTQS CONNECTIONS --SSHHEELLLL- IN VT OUT 3a7* -channel-in OUT 3C CORROSION ALLOWANCE -SHELL SlOE ISd CODE REQUIREMENTS AA|AE g6X."nOl VUIPlTEW* WEIGHTS - EACH SHELL bundle CLASS RATING 5QO* RF RATING 300=* RF TUBE SIDE */fL* - full Of water SPEC. imi NOTE 'INDICATE AFTER EACH' PART WHETHER STRESS RELIEVED tS.R.) AND WHETHER RADIOGRAPHED I X-R) -? S.MA - q> Bajcflel SPAsCiMza S*/?.". BA.rruE.CuT?S% w . >Qto- A <>ATE A **** RE-VlStDjs t*uW>Fak. Cwuvrf2S i*6ocD For Purchase T*.* ** tP" JOB-NO. QRWG NO. I'REV. H'-5-E-lj 1 | 100^5 WA-TEX 000413 FORM H .19S PART S 9 /6 6 t EXCHANGER SPECIFICATION SHEET w> 4 a 6 CUSTOMER AND _ ., PROJECT_ LOCATION____ Tg~X. A.C.O INC, plant" .1_____________ Puacri SbuHO exchanger no. `-.,5 TrJBLfeg. s.tRV]^?. F UNIT DLPROPKHI1.ER. &QTTPHS OtOOUSuR SIZE * 24-0YP KES____________________________ CONNECTED IN SURFACE PER UNIT - 74& EFT. *4: SHELLS PER UNIT I EXCHANGER _ REW. NO. ITEM NO E.-Q3___________________ SERIES SURFACE PER SHELL PARALLEL 74S EFF <nfc 7 FLUID CIRCULATED__ 8 TOTAL FLUID ENTERING 9 VAPOR 10 LIQUID 11 STEAM PERFORMANCE OF ONE -UNIT SHELL SIDE TUBE SIDE DgJ=>OPA.MixPZ StfAS LtsJm 4>A5-7. Coolinc, Water *73. OOP .Ta^o (2 NON-CONDENSIBLES . _ 13 FLUID _V_ A_PORIZED OR CONDENSED 14 STEAM "CONDENSED' IS gravity-liquid Sp 16 viscosity - liquid -<=E- 17 molecular weight-vapors 18 SPECIFIC HEAT-LIQUIOS 19 LATENT HEAT -VAPORS 0.514- <1m^ ~ <j>55^fOuY^ O-n n*r>-Q.I4SgoJr> B. T.U./4> B. T.U./ B T.U /* b'tu/# 20 21 22 O' 26 27 temperature "temper'at ure IN OUT operating PRESSURE PSIB NUM BER OF PASSES VELOCITY PRESSURE DROP ALLOW/CALC. FOULING RESISTANCE MIN. .ISA. lOO J^SL 4/4 0.001 FT. /SEC. # /sq.m. 7G> IQO 40 12 / 12 0.003 FT./SEC /S0.IN. 28 29 , 30 ^ 31 i 32 33 : 34 35 36 37 38 39 HEAT EXCHANGED-8TU./HR U7SO.OOO W T.O. ICORRECTEO) JLSb^_ transfer rate- service 75.S CLEAN ACTUAL FOULING FACTOR C 0NST R U C T I 0 N DESIGN PRESSURE TEST PRESSURE DESIGN TEMPERATURE TUBES ImH kptA NO. 153 300 450 >50 oo vjp PWO, V<ff */so.i. IP/SO. IN. F tBL LElWTM 150 225 300 240* PITCH I*. */ SO.IN. */S0 IN *F ^L.Cabbom Steel SHELL-CQVER I. D. THICKNESS floating heap cover C.P.RBOM Steel CHANNEL CKRaoM STtEU CHANNEL COVEN CAvR-ROM St&EL. TUBE SHEETS - STATIONARY HkV<L\ R.O*-\_gta ' FLOATING V4A.VA.V. gouL.E.0 BtASi BAFFLES - CR055 CA.RRQH ^rggul TYrc Sg^M08T-A.L-<>TH,^FNESS _ ...... BAFFLE - LONG TYPt THICKNESS 40 TUBE SUPPORTS. 41 GASKETS ME.TXL. JXCHgTEO A.SfegSTO^ 42 CONNECTIONS - SHELL - IN our 4L 43 -channel-in 44 CORROSION ALLOWANCE -SHELL StQC OUT >/k 3E THICKNESS RATING 300 RP logP. TUg 5IPE _______ 45 CODE REQUIREMENTS A3MC 5N.C.TIOH VUIOITEMA CLASS R SPEC. &tM1 46 WEIGHTS - EACH SHELL BUNDCC FULL OF WATER 47 NOTE INDICATE AFTER EACH PART WHETHER STRESS BELIEVED IS.R.I AHP WHETHER RADIOGRAPHED Ix-R) '4 I jljfj<Sl^l},...BAPFLK &FJkCtM4i SH . BakP-PUSl CI.|Qflb---------------- -------- - 51 DATE 0si ftEVI^KD,, |60El> VoC CoMST T4** Llasucp Ppg Porcu^^a JOB NO. DRWG. NO. I REV. & too^s ` Js--^j I M WA-TEX 000414 10.4 PUMPS WA-TEX 000415 s TABLE tO.4-1 fJGAL PUMP SUMMARY SHEET POLYMERIZATION UNIT PLANT 5J ^CORTES. WASHINGTON DRIVER DATA Full Rated RPM H.P. Load Type _ Amps 3600 15 Motor W. V', ^ * h- 3 * Ig- r I *. 3. r ' WA-TEX OOQ416 2I % k -J i CENTRIFUGAL PUMP DATA SHEET E.ic\s.Tvvia VisvaP job no.U2DS_item no_5 3ju_r 3.._________ PURCHAIE ODDER W.JLQ -O ^.S. .ft, ~ O "2- APPLICABLE TO: PROPOSALSO PURCHASE^ AS MIT O NOTE. < J INDICATES INFORMATION TO K COMPUTEDIV PURCHASER: BV MANUFACTURER Kaumrnm^l^SfiS * b~Q% mourn m.-------------- . BATE--1--2.. . REVISION FOR rEShtAcC^ fAJ, ' UNIT Ct^-r. PQLy SITE____i NO. INJURS MO O NO. MOTORS RED DJbrLITEM No55=QMlS PROVIDED irSjUSBrt'Xfc^.MTD IT... PUMP WLTUIWlE(ni_^_____ ITEM NO.____ - .. FMWIDEOBY . _______ MT08V _ --.............. - SNSPttB SHE AMD TYPE J-t2.iJLs l^TStSERIAL HO._ A-Sifc) OPERATING CONDITION*, EACH PUMP U0U1D----- WATigCL. .... US PPMMPT NON 1*10 RATED - OISCM. PRESS, P$N_ _a&x FT. F. NOR. l .MAX.--------------- SUCT. PRESS-PSIB MAX____ -RATED- _L _SP GB at PT_ b -------- ,-------WFF. PRESS- PS 172* VAP PRESS. MfT.PSA- fi----------- WFf.BEAO.EI______________ VIS t PT. Sm_________ -CP---------- NPSHA. FT~2L M JL$L CORR/EROS. CAUSED BT.._ -HTD.HP CONJTJMJCnON^^ PERFORMANCE /fiT PROPOSAl CURVE NO_fill'iCfcJW> RPM-155Q___NPSHR (WATER)JLlifef.. EFF.___ S3____ BFtP RATED MAX BMP RATED IMP 5P5T$_______ MAX HEAD RATED BAP MML CONTINUOUS BPM ROTATION (VIEWED FROM CP16 END). SHOP TESTS NOZZLES SIZE RATON FACING LOCATION Own. PERF. SUCTION .360- _ RF _ TOP .. ... Own HYDRO DISCHARGE __ l.V-3._ ONPSRKO'O ___ _RE___ __ Tap--...- OSHOP INSPECTION OWIT NPSH CASE-MOUNT. CENTERLINE FOOT RACKET VttT. (TTPEI-. OOISMANT. AHrtP. AFTER TEST 'SPLIT' O AXIAL DRAB: TYPE VOLUTE OS61 DHL DWEFUSER PRESS: OMAX ALLOW.PSffiT: DWORD TEST- __PS6 OOTHM. -CONNECT: OVERT OFRAIN DBASE. . .. IMPELLER OlA.. DRATEO_____ ? *` 4^ l~>MAX______f.&Xl______OTTPE:CU2&S MOUNT: BETWEEN MBS OVERHUHB WEAA.RS.OIAMFClItNC______________________ BFARLNGS-TVPE: QRAWAI______________ DTHRUST LUBE: OWNS Oil 0(1000 Oil MIST DFUHBER D PRESSURE COOPtlNS: DMRFOM0MI DRIVEN NAIF MTD IT: OPUMPMFI ODRIVERMfR O PURCHASER material# AN CASE/TRIM CLASSO-- JaBfttf.Prl _____ ghatr-cr SHAFT- UlUO -UT PACWNS: OMFRATTPE! StZt/NO.OFRMBS- MECH.SEAI: MFR A MOOElAPICIASS.COM___________________________________ BASgtATE Q. MFROCDE- VERTICAL PUMPS AUXILIARY PIPING O CW. PIPE PUN- -OCU: Olt: OTUMNB: Ofipe_ O TOTAL COOUMB WATER REOU IPM- -OSHHTFiREOrO. OPACXINB COOUMB HUECTIOd REQTh DTOTAL BPM Dps8 OSEAl RUSH PIPE PLAN.OC.S. OlS. OTOWM OHPEOEXTEBNAl SEAl FLUSH FLUID QBEM______________________ OAUXULARY SEAl PLAN _ .OCA OW. OTOWNS OP**E_ OAUX SEAl QUENCH FllllO- M0TOR PRWSN DPMB- pitorsumpobthO____________ ___________ MM SUBMERGENCE REDD. ____ ____________ COLUMN PIPE: O FLANGED OTHREADED LINE SHAFT: OOP** O ENCLOSED mbs: dhwi_______ dune shaft -- . MB LUBE OWATEN OWL DCREASE FLOAT ARM OtS. O&B OMZ ONONE FlOAT SWITCH O------------------------------------------- PUMP THRUST, LB OUP- . ODOWN- t i t n m v ossfAwr oci Oft HP . RPM_ -VOLTS/FHASE/CYCIO. MFR___________ -ICANNIS- ___ LUBE___________ TYPE----------------- -IN4LX- -FULL HAD AMPS- INC- . -- __ TEMP RISE.C_________ .LOCKS) ROTOR AMPS- OVHS ovss VERT. THRUST CAP-ll_ . SOMCE FACTOR- APPROX WT. PUMP I BASE-----------------MOTORTURMK_ &ig &EfcgJg.API STANDARD B10 SOVERNS UNLESS OTHERWISE NOTES ,firXl*iT\ vAO-BijAg , -MaP.1FiM& gggUC3 - MBIO lNA,B>eL-L.M.TS% Vs3f?Air. .< $ ----------- i1 o U'lo-v NO. DATE ISOO. PURLM^I? FOR OIJnTATlDKl JOB NO. DRAWING NO. REV. m A r* 0 fa IO03S DS-5H>- 1 SHEET J .OF----{------- WA-TEX 000417 ( CENTRIFUGAL PUMP DATA SHEET O O OAPPLICABLE TO: PROPOSALS PURCHASE AS BUILT job no._^5~v7; PURCHASE ORDER NO._______ ________ __ .. RKWimoiHa.JJ3_C>C>\ NOTE. UIHOICATES INFORMATION TO K COMPLETED BY PURCHASER- tuauiiiv ho.__ l....... .......... ..................................... BY MANUFACTURER DATE___________________ REVISION................. T' F ' /Ayr:FOB,__j___u__j_s____________________________________________________________________________ unit ...CAT*/yr/t: bxva-Y/st/rAT/o/J______ service ___________ _________________ .. as/*&/? /=&&> SypAiJ .7-NO. PUMPS REffQ_2_.N0.MOTORS REOD.J_ITtM NOiff 662/A PBWOtOVU/$Lf,ff^fepITO Vt -&.&1 fZ. _ PUMP MFR. NO TURMMES RHTD -- ITEM MR -- . PMMIOBY________ ,,MID BY- . -TA<7AorA sat aw type /.vX ZA/O'&tfySJZnxt no. _. ... OPERATIMQ CONDITION*. EACH PUMP LIQUID__ d-Z'.3/-C4 - U S PM t PT. NCR- &S,..___RATED- PT. F, N0R.Vj2c2_MAX____ .bsch. mss. rsm____3&3L. SUCT. PRESS. PSIS MAX. 330. RATE8- SP GR. M PT O. 4-75 -BFf.FRESS.FSt_______ -ZZL VAP. PRESS. M PT. PSIA. .Z3tZ.___ nFf.HEAO.FTVtS.itPT.Sw_________ --CP^cvLnPSHA.FT_ 376 Jp.ZO CORR/EROS CAUSED BY- -HYD.HP- CONSTRUCTION PERFORMANCE SRJ PROPOSAL CURVE NO. RPmJ$5w2.HPSHR IWATTRI . EFF. <33% EHP RATE0_F^2L__ MAX BHP RATED HAP. MAX HEAD RATED MIN. CONTINUOUS CPM. JjSL ROTATION (VIEWED FROM CP1G EMM SHOP TESTS MOZZLES SUCTION aee .... 2?.... RATNM FACING A?At LOCATION DISCHARGE \3c>q& jBj~ _232/?- . CASE-MOUNT:CENTERLINE DFOOT OBRACKET OWAT. (TYPE). SPUT: AXIAL JjjftAD: TYPE VOLUTE Jj&8l OBBl QDIFFUSER PRESS: nutv mnw tr*j*7 **" f' HYDRO TEST me OW1T. PERF. $$W1T. HYDRO OKPSH REDO. OWIT. NPSH ^SHCP INSPECTION OttSMANT. AINSP. AFTER TEST OOTHtR........................... 5MEL-CONNECT. INVENT IMPELLER OIA_ RATED- w-caft. MOUNT: BETWEEN BAGS SjlWAHUW WEAR RG. MAM./CLRNC- BEARINGS-TYPE: RADIAL /^2532/OjL#. DTHRUST/ LUBE: D RING OIL DFLOOO OOIIMIST ptfLINGER OPRESSURE COUPLING: OMHF _ _______ :______ D MODEL-------)Q. DMVEB HALF MTD BY: jgJPUMPMfR ODRIVER MFR OPURCHASER TYPrfS/aBfiCr MATERIALS API CASE/TNM CLASSO_______________ &.&MS. - P-. 2M 7. (ZSMS__ P-2 A /. PACKING: nMFBATVPf , . . DSHE/NftOFRMBJ MECH. SEAL: D MEN A IWDEl^&S^rjfe^S__APIL.y; MFR OCOE ___________________G?J3r &T BASEPLATE: VERTICAL PUMPS AUXILIARY PIPING Ocw.pipepi.am -- QCU: OSS; OTUBN8: OPIPE_______ D TOTAL COOLING WATER BEOTL RPM Q__________ . OUGHT f.I.REOTO- OPACLINS COOLING INJECTION RIOT* P TOTAL 8PM DPBtG /?,OSEAl FLUSH PIPE WAN OSS OWBRG OEXTERMAl SEAL FLUSH Rum OBPM. DFSIG- OAUXttlART SEAL PLANOSS OSS OTIMING OP*PE. OAUX SEAL GOERCHFLUID US ATEMj gfo Ao ffeftg- HP -/iG* MOTOR ORIVIR MANS^'/WVJ VOL MFR.--/gLC_________ BEAWN6S- --tl TYPE- r- ,~---r .mm .FULL LOAD AMPS- nc TeS'^CLtemp rise. c<32_aoa<EO rotor amps OVHS ONSS VERT. THRUST CAP.LR-- LERVICE FACTOR- PITDRS0MPDU7HO. MtNStSMERGENCE REOD.D____ ___ ______ ..' COLUMN PIPE: FUNDED DTHREAOTO LINE SHAFT: QDPEN EHCIOSEO IRDS. BOWL DUNE SHAFT------------------- BBS. LUBE QWATER 008. DGREASE FLOAT A TOO OC.S. OSS OBBZ C>NON FLOAT SWITCH D--------------------------- ---------------- PUMP THRUST. LB UP- . a DOWN- APPROX WT.PUJMABASE- MOTOR .TURBtNE- APISTANDARO *10 60VERRS UNLESS OTWBWISE NOTED- f 1VW7* 0 \ SS.uLiTs Cnn OliotatiOki NO. DATE Jfll si jor no: DRAWING NO. REV. w-$<3vq*l \ SHEET . / .. .OF--|----------- WA-TEX 000418 FORMNO 1)0 <RC(VSCOAPRU 711 ( WA-TEX 000419 t I WA-TEX 000420 ( i WA-TEX 000421 Byron i 10^5 INSTRUMENTS WA-TEX 000422 kT*' n;,' 3Nf'*FZ w / ,^ j*i r3i# * % j f*1'' * /:- v ' -* , '"'*^5 '*^a? `^7%'\. -r %&**% -'Vf.fv ; :' . - *. - '_ :b.^- ,3 ; 'i&M , fcK.,a.#fe TABLE.lb.s-l. -"> ' '- ' p*" Element No. .'" ' 'V'' ,'ili 'S-S-s. ,' . .. '-. -v. V.3'v >; ' ; v\ : ' '.'3~..S*bK; ' - * `.'W*'*'/' ^ ,*'. VFLOtf ELEMENT.SUMMARY SHEET rV dATALYTtC POLYMERIZATION UHtT PLANT SJ AHACORTES.. WASHINGTON. Service ' ,v * 1. ** . .. ` .;.v- f..* 4->*3,v. * ' .' *" v**.. ..*'v'.>%i'"; ' - .a' `:V ?i - ; , ' ';' Orifice Sl2e Line Size Meter Coefficient 5FE-19 Btms. Cooler Outlet . 8*'C r . 2-132 . 5FE-200 ' Amine to 5J-C57 . / - 1.978. 5FE-Z01 Caustic to 5J-C59 1.238 SFE-205 Oeprop. Feed Bypass ' 1.123 5FE-206 Stm. to 5J-E58 1.959 5FE.-207 Oeprop. Reflux . 0.901 SFE-208 Stripper Vapor Outlet 1.923 3" Sch *0 3" Sch 40 2" .Sch 40 2'-' Sch 40 3" Sch 40 2" Sch 40 3" Sch 40 40 BPH 15BPH 8;BPH 8 BPH 100#/Hr 4 BPH 4000 SCFH 'v- , >.. . ` .. ' *,v- . -^ %v~' ** . .y v* .. .v.'; .. . *- WA-TEX 000423 3 | Tag No/5PSV-10! 5PSV-102 5PSV-103 5PSV-104 5PSV-105 5PSV-107 5PSV-220 s* .* " , ... / "J " '' Service ~ _ " 5J-C57 - ; ' ' ' 5J-C58" ` ' 5J-C59 , 5J-C60 5J-C61 53"E > 5J-ES8 ' Size 2*' x. 3" .1 M. II ' 1-1/2" x 2" 3/4" x 5" 1-1/2" x 3" Set P.ess 310 PS1G - , '* 260 PSIG 75 PSIG 65 PSIG WA-TEX 000424 f