Document 3e11R82Ma5j8qn57oKOXVOVxy

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  X , -v '. \ ! ' Tr 1. GENERAL description WA-TEX 000377 vsl. "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 { 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 depropanizerj 5J-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 5F1C-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 (Reference-PSlt). 5-RA-5):-.; The amount of saturated 03-04 from the f#ed preparation section that is pumped directly to CRU No. 2 is-control |ed by-flow controller 5F-I-C-205. When the propane stripper,-5J-C61, is I ^..operation, a vapor product will be leaving the depropanizer-propane strapper-system. For this case, 5HCV-6 and 5HC-20 should.be positioned sgch 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 condensers, 5J-E13. Feed to the propane stripper will be regulated by flow controller 5FTC-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 thp, depropantzgr pressure controller, 5PIC-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* resets the net product flow con troller, 5FIC-207. Noncondensibles may be vented from the system peri odically by operating hand controller 5H<i-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 of the Operating Manual for the Catalytic Polymerization Unit. ). The temperature of the propane stripper bottoms 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. i WA-TEX 000383 3. PREPARATION FOR STARTUP WA-TEX 000384 Ill - 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 procedureis 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, 5d-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 "0-162. 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 ' "y 'v ' '( 6. 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 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-10* Saturated C3-C4 Salt Filter, 5J-C60 5PSV-105 Propane Stripper, 5J-C61 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 4* ' *T! : /v *A *v- '^r-C.Y ' v*V ( . 10. appendix , WA-TEX 000393 10.1 PROCESS AND UTILITY DIAGRAMS l ; WA-TEX 000394 ( PROCESS FLOW DIAGRAM 5-RA-1 ' WA-TEX 000395 I PROCESS FLOW 01 AGRAM 5-RA-2 ; WA-TEX 000396 f^iura _ tfyc&l 0iaE5IGWAW0M. * Mlr.mcac>hiu) t -T ' aSnfttoou nwrawc t 0CUT?L*u?o0* TBtAC# t*>T. 99IP SVMfrOLG ----------- -- t * * -A--&-A o-r-e-- ^ CtlS7lN6 New fteUpvft Mlfic&tt wor useo -donot atMcve. OfiUtfT** Tie-inWUMftfiR* A Mgrgft I, ZlVitUPH* Of Uijoa 6Vfrf.l4i Afc 6>l6NATEt> (*w TN8 swowm Abo**. mimoo. j REVISION* ARfc ClftC-UtP AWP.IUCt.UPfc & TfclANPULAJU REVISION MARt. fl; ptPjNC* GEftviCfi SPECIFICATION* POE. N8W UNO Aftft IN */UfcOaDAwC& WitH <htM5 J'70d . TAbut T, J, Uwt Vigl *UPPt*t* Fofc IU4.Ut.Mi0N ON NEW - l(Wf* ARC IPCvTlPfEp A* fcOLLPW*; Pp PE 8 SONVEu PROTECTION cc CO\,p CONSftRvATI.ON. * PMC PARTIAL MEAT 0N4CRvATlOM . PMC PULL UEAT C<?N6CVATIPJ . OTC OPERAUMfr TtWPeO-ATUIL& CONTROL *T 4T&AU TOAiEP t iNfut-ATEP Ml . UP WAUuATieN LINE IDENTIFICATION 'Tt* ij-C'-iiaA-m , f f t-------MSUtATION yv TEXACO* {Uftfc SIZE 1 ACQUIREMENTS iA ass, &$ . WUMUIt L TEXACO PIPING MATERIAL SERVICE SfEClMCAflON ll i -0 P* ___ A k- * * i. 5v--ajuir-*i: UU r>B| jj Stouutr. -. |5*flll r1 i- fe * :" ' 90-AW*S<* gt 'k | ' /-. $ 1 mm 4- Pit <& t-t-7S REVISED S-AAMOl PER DRAWING REY.O PP 4* r<k. a&pso ujilrry siwon *t*** % 5 %ST-ST-I *lh*jfti-PN& V P S 4IMUtO POt CONStaUATKW 2 - 8**> WPWTEO T s AWMO ISSUED FPHAPPWVlL . . PHS # .Mb ** ft eu rs i* a *m. MALI | attUMft nun . BEOlim mm iHO. PUOCT SOUND RLANT mm. UTILITY PIPINGS INSTRUMENT DIAGRAM STEAM i CONDENSATE SYSTEMS CATALYTIC POLYMERIZATION UNIT .>1 *MMk w nt*m- iee nuatn- ssio *n4. w. 5-AA-7 [1A WA-TEX 000397 t s r*i -c 5. H* U 'muz sTaattg t t)f?h\ 7sT A> JM RpifioY*>il/s**r/P0Matmrnt.M9*.#***v*l<tjnJ;.*ff*tm*TCT Is UJ.*.*L. tssu&o roa.constjmciiom !a>/ UI8PSP0AKTDCRDMTOAm40e6vAAWLAKD ^i&r-zr ]>* *ssf*^7r.i.*' Lll BEOHTEL 0%$ TEXACO INC. poctr jouno runtn ^ztaktai** PLOT PLAN CAT.POLY. UNIT Kbrni- Km StM nuuin* jo 5-AA-8 J5P * WA-TEX 000398 MHC. CfttCulH) .cm wombeq iStlJWCl Otiieu*H*f iwo <t.f.c<j.) XI >0U,PU6LQfl.& J`0>70& , **. 5*-o-r** * *s* y,-7*"y*-/lf- -6-C, 6-- -0-0-0" O Ntrv REMOVE RELOCATE MOT USED (DO WOT REMOVE) DEMOTES Tlf-IN NOM&CRS MOTES L REVISIONS OP MAJOR SYSTEM* ARE OeSlSNATEO C7 THE SYMQOtS SHOVSfM ABOVE. MINOR REVISIONS ARE ClRClSO AND INCLUDE A TRIANGULAR REVISION MAR*. t. PMN& SERVICE. 'SPECIFICATIONS TOR NEW LINES ARE IN ACCORDANCE WITH GEMS J-*W, TABLE 7. $ LINE NUMBER SVFPiXtS FOR INSULATION ARE lOEHtlflSD AS FOLLOW*: PP PSRSOMMEL PROTECTION CC COLD CONSERVATION FMC PARTIAL HEAT CONSERVATION FMC FiA.1 HEAT CONSERVATION OTC OPERATING TEMPCRATORE CONTROL ST STEAM TRACED Ml MO INSULATION line idenTIFIcauon ............... J'H l-6-J13A-M T f t--------iNSUlAttON A TIXACt^ TEXACO $l { tE6t/IMM{NT$ AK WANT PXIMttt seavicf 5YMI0L t-NUMEU L TEXACO RlttNO MATERIAL SERVtCfc SPECIFICATION *--* i III %Y< 00 U * ** MNMKM .. ft L KM W,4-`iwflP*H rc M.H 1*. pciAw * 9P LLH Ir^nrr*1 SP 5l {tfijraSsH IP (I l |c5i|^| " Oft tt&MssI*** men __ fer 9. < JMT DU6SUM ?Ts:fe?/s 4T --- - M-iow;. S] ---------------------------------------------1 4 AEVlSfiO *=Eft ORAWII40 VAA-HO RSV.lA Hi REVISED Pft DRAWING 5-AA-TJO REV.O 1 l *p 1% B- IE*1 $*! J& \ ft-'s tmo ftp*. eoMstautTicN 't 3Si y_ JL &4 UPCMNTflO TO JO'S ObkIaAp ISSUED Ptf>e APPROVAL ?A i jfc 11fir <IWW v tij kw>. r- SB 1 ___ _1 KHt HONE t . ___ IMARA . ...__ BEOIITU HDUStOH TIxMom toatr souno plant utility PIPING < INSTRUMENT DIAGRAM Am t SLOWDOWN SYSTEMS CAT. POLY. UNIT 0 tttxm - iom *** 5-AA-IO nuttUt* 3tl5 b. I1A WA-TEX 000399 nil'OU IA *u **mM ! tvctt&Mr > C' DtCMTU ->0095 7CXACC EM-3910 SYMBOLS G-- IT EXISTING NEW REMOVE RELOCATE MOT USED (DO NOT RE MOVEJ DEMOTES TIE-IN NUMBERS '6 tiOT5 . RYI5I0N$ OF MAJOR SYSTEMS ARE DESIGNATED &Y THE $YM6<X$ SMOWH ABOVE WfftOR REVISIONS ARE C/PCUD AND >MCLL'5E A TRIANGULAR REVISION MARK. t PIPING SERVICE SPECIFICATION* POP. NEWVINES ARE m ACCORDANCE WITH GEMS J-Odf TABLE ?. I VINE WJMfctP SUPPIXfS FOR INSULATION ON NEW ARE IDENTIFIED AS FOLLOWS: PP PERSCHWEt PROTECTION CC COLD CONSERVATION PNC PARTIAL HEAT CCW5$RYArK>M ' PNC FULL HEAT CONSERVATION OTC OPERATING TEMPERATURE CONTROL ST STEAM TRACED HI e insulation y|A. A LINE IDENTIFICATION mY ' "?"* ABB ITMBOL T-i"-}\3A- HI Stlit j ' *---INurSOUULHAklTMIEONNTS [ TEXACO PIPING MATERIAL -NVMKt SERVICE SPECIFICATION A M- VQAi S-fti* > s.iu* o ' %.*4-10 M-3H > )<U-I L S-AA^S ^Tses-i U----- ---- .X -H 0 SO>M A A ftV'7> REVISED PR DRAWING S-AA-IU R6V.O a >OD#D uYluY-f SlAftiLi % \fc WP8M4T V>*LVS $'OJUtD OBSTRUCTION ftit ta\ A % UPDAt0^> Jb AvwS15 HrtOEO F0EAW1EO&1 fs* - *- fciMiO A o* StM *- t*. w*u 1 CtVIMO tun BECHTEL HOUSTON TlXMOlHC: WOET SOUND PLANT UTILITY PIPING i INSTRUMENT DIAGRAM WATER SYSTEM CATALYTIC POLYMERIZATION UNIT &***. 5-AA-I 1ntwn- wc*a mutn- Mio BA | ! WA-TEX 000400 AMIN. Tt-GEWfcRATOa. AC ,-MUUATOft ^oVaA'-o' ft* 1 x-v ' X1^ *v-v* TO PttfctWf*-* . W*M i IvL.... MM ny|.i -4 4 6 0COUTOOt V/U.VB <AWT (OBAN OWAltOUlVOI) - SPlCJiCti LIU - onaiTiettAL CONTROL VALVC <CLO*t OUMO ZAIUMt) --pT)-- i*ltutu BUMP TEST OAKTCY VALVE P )N&Ut.AT<OM RWWOMuttPsoncnew 5 60JMSTRUMENT YM LS & 6 00LOCAL MOUNTID OA .Mouwreo . l bamsubb tmt J TQANVMITTtR TOLANT WUMDtft -jmttRUMtUI IDlNTiNCiTlCM 4f>>{u4gMTftAuHUeMMto4rUPMwBmWtmftay atHtta |>MS7ftUMENT IPtMnPtCAtlOKt iIM>7tAUtuSAtrAat>oL M^C/uIPr*Tkt<i oMo>eToWi`u, jA*ccUoyamo*wMettriftwtoitWhA.MO. u UMfc MOEMTIPICATIOU AMB MtSSUfit woo MT 66 a.ttXj^jjTL^u 1----twrf MUH U AC. KAMT V*j} *........ c 1. I--.1. *. tt l ca >UUI US f pcmovc r-&-- REtOCM-E t NOT c*SEO <0j9 NOt PEMOVg) 0 0CHO7&6 7ie*m mtMBens NOTES I ftV(5IOHS OF MAJOR Y5TU$ AR OCSl&WATeO TME S^M&OLd OKCWH ABOVE. MINOR REVISIONS Aftf ORCkED AND iNO-UDE A T0tAK4ULA.A REVtSJOM MARtC. P1PW6 Service SpecmcAricNS Ron he/ UNIS ARE IU ACCCRDANE WITH GEMS J.2C6 TABIC 7 * UNE NUMBER 3URRIAES POR IN.SULATICN ARC IDENTIRlEO AS FOUOW$ . PP PERSONNEL PROTECTlOK CC COIO CONSERVATION pmc partial heat conservation PWC FOU. MEAT CONSERVATION QTC OPERATING* TEMPERATURE OOUtfttt, ST STEAM TRACED N! NO INSuLATlOM 4 d* fiHCATg mcp *uoiwi wftatCMnutX v W4C-79 -(y'.'47bVt>- ... 77J7- CssL^gsssft- '.PfytfLmtA *53pgm ---- Iy*'-** -tJ*~iifc'r /,. j .5**- <y.j.QQ3)~ =^, ^VirL'jT-- -^<ess: T >1 SSEE?~ 7 togjmc ttAfig j Wyp^9CAg6<m,uagtgtftviJ>4 ~ VfcM sfeMeeay PQAii VATU. ItUMj WCtUA7fc fwmcwArta M>OlFVyB Cfr.6ATCV4tVt 'fig B.F. I jOOlPieces.GATgmve Ste*C>RtCPAWgj3X ca SQUAt, * 30of.Tt6t> C.S.GAT YAlVe Vj&- gj;,CgAU 33*g 00 CQtUU i 30OjFLOP (*>. 6*1C VALVE %6* C.R>PACIFIC350-Uflglfiuu. jogr: PUGWVC VitfO.C.WgPMgK OPCfiATEO 3C3tri<y& CO. LUB.PtUOVAWt wtHCM OPtflAltP Mom .t iMiuUfr!0malxriVtficiM*4kl (UC^>aW-atrt>j-6>&a? roifQtiogK . t jikuoet fro w 4JU hub. . <Ki--r..^^-Vrwai| VAtitl, |Mt ro Mt>+ AgCOAP.WtT ^O'A'W't) fftCFegewcg eoAvitJc^ 1 UTKirV P/I.Q.^TU gCOxg.^vareMO. CAT. POLY f ttAt *TtR tV ^g.yED ^&JuUo tOUUgCTlOU $ ____'aomo V acAucH$6 utw?^v9;-a*tov (uuq 4%*ai r 7g> *-um* :yi ? b^TADOtO OKU>6TTft|AMUC: JtSC&u* ACCUM.* W-Cjci f ^,Si^4K..4r^84iv.iC?p'`'li *OM^* n ; J-A-` ---7J ntflMBMCMKAUMMCQLL, TTfOt fjcjMuASUltM.,lfc. i UvKO__tT'Si'C_VAVf A Bv-^v 4AOCQ ttlA. UcUtWtt1 *CT % PiPiwa. ^ <& 6w?t4 A#cc P6v*>?| to t ----------- _ ... ^ SEE^O A 6U'Z43 mcormxo 4jzc Am D^>o-i<a pooi4 a*7a4*ii RCVIg^^TOOXfrSjMg. .. * m** Ai^6Paft<aarM6><ggo3rc*crvh * KSCHTEL COSPORAHOM UNIUNOKO THE TEXAS COMPANY Vuon sow* wows paocc&s pipjwc 4 JusmuMiwr siacdah Ft> q?ARA7tOU StHTlOVt CA.TUY7IC P01YMMIIATI0M Ur 2525 " krw*< a ^'i'ij v'VfcTf""T"---- ~7TL- iVt ' /DO^O'ST TO Sj-C-61-3' ^ ^ REVISED PER ORAVriHS RA "rS`AA-iOA -RgV.O T5C t**CS*' VI ^Ts4*i^aT*-s *~T ' %T tPWkTKO Tt* a>*axD < ^ Ni- ISSUED POR APPROVAL 7i > T'. %i >t ff 8" ! rr * f t l,il 2 _ TEXftCJ IMC. sr .... PROCESS PIPING $TnST' DIA-'..,A^ FEEO PREPARATION SECTION ._ CATALYTIC POLYMERIZATION UNIT M>t . -- ! 5-RA-4 m WA-TEX .000401 ^.Vv^jS s'- 'iv P O '' 70 RELIEF HEAOC* JM-RF iT*2}P } ^v-ioaHS '. \ /50*S1-G*lVnt->ST r 2S3> SSt~5.J-BT*S-I-4I2PP ^ SJ'ST-ICJ-f'UIt-PP I"--'-' - -4- Srtcuac ftuuo OPftOAT OhAU -5U LOMtBOl VALVE '> suvtt cv>aci wen <ClOSt OW Aid FAJUJtt) 4-ihUurw* jtuw T*t4ct> pp.^ajcnuk. momittx SMClACU ftviWO ti jU46TR0MMt SYMBOLS MELD MOUNTED M ftOJkfiD MOUNTED P81M. UME&M>C. CCMU mvnatwiftto. AAuvit TuSitviiicitxA^viAo tMniUv tywH5 -DUUT UuMbfcR /$M\ lUStOUMCUT IDtMNMCATlOU \3V--- INWHUMENt UUMDEJZ IU5TQUMEMT IPEMTIPICATIOM ail iu*nuiMtwf& ABftcoeepJM accoadaucc with i... STANOAltDS EXCEPT AS U0tfc:-T MUTS Mil* TO **$*90>W` UM6 IP6MT1FICATIQM toft uvtv wHtat vilqciu* awd musua* orob him m cauwund PlPlMfr SP*C," flSJ-q-Tg t-iimE SiniAiNl .c n>WTW*J | L-~ COMMODITY L---T T. <4. OtM Vi> rat imtsiv*** smavue *ct nQuigms wBtn mop cAteuutiOM? -jom PlPIXtr maWATJOH PIPING SPECIFIC ATIOW jtw-MS iooCM. ftAJiwo. vy toan.Aucw. RELOCATE -0 0-9-' NOT UMO 00 *r RCIIOVCJ ' ^ DENOTES TIE-IN NUMBERS J NOTES { . REVISIONS Of MAJOR SYSTEMS ARE designated by the SYMBOLS SHOWN ABOVE. MINOR REVISIONS ARE CIRCLED AND INCLUDE A Tft/AHGUUR R&YlStOW MARK. f&.PlPlHG SERVICE SPECIFICATIONS FDR NW LINES ARE IN ACCORDANCE WITH GEMS J-D* TABLE 7. 3. LINE NUMBER SUFFIXES FOR INSULATION ARE IDENTIFIED AS FOLLOWS* PP PERSONNEL PROTECTION , CC COLO CONSERVATION &. PNC PARTIAL HEAT CONSSRVATWN FHC FULL HCAT CONSERVATION OA.OTC OPERATING TEMPERATORfc CONTROL ST STEAM TRACED . H* NO INSULATION ?4*TCOGOOSRNASKVOEEItTETNPYtOCNALytSBROMSRUSST?VCTS0AHF1RAFBSNMOfoW,N*TA..HFTREUEOORSMU.AIEDINLTCtPRPtlMfS>CPM*ESCSUIMFAIAMCLL i /E.SaIjMBST-tRbOaMcac+dJT- STBAM TfcACfc*? J&YMEBOUS* * Q^-TlEACaO 4 MOUSBO ^ ^ -- - LINE IDENTIFICATION rrv4,9- S'-ltOA- i\ t TEXACO' HX*rt I rfISMHMIML PL .l I 'Aft SStTMRSVOi5fiL.UI MKK l Pivinv *AA1a0lt SetYlCt 4 IwTlCATlON a A i--- * 40- SID )SOt<L GAIlTT^ft' C08B. AUOW 40-SSD COCKS, VKf C0AR.M40W. 40*bl6 JO*SSb ;o.sor >OD*P^ SATES, VlB* COOR.AUOVC SOO^R.?, COCKS,Mo*CORR. ALLOW50* jm. cetmji.o' coxk.^juov. COMMODITY DLSISMATION <0HDtH3IA MTCX wKUmXCCruttSnCN94LU{QWsaBl PA hum I etwwHan ITEM NUMBERS )99rU6tt.(.9..QAU tAlVt Vu H.f. !l9*HIP,C.|.>fU>& TAWI Vu'lLA 6*mitST>`-^a-i^3>3 -------------SE552> BEFEREMCE PRAWIMO& oaociw o&i.o.- rtto patRstcT. cat. poly, vmr oaoctss ci.o,-itmToA-Mcr.aAooLY. wrt tillLlTV^RS LP.-S STEAM C COMOCNPAIE OYitCMS UTILITY P.Ol,P. WAItH SYSTEMS unury > a i.p a> & oiowoowu VO J.0.7AUHA& CmunCOHVECTINA LIMAA. BKT**t PlOT PCA*CA?AlYr/C X4YMtftUAT0U UNIT J*BA*A i-a a>p riAu SAA40 TIRA> JAA.#' `nwi1' <S-BA.-4< MOT> l Sim. TftjciN#cT vissil torn toil mAccoanhcl wtpi Oiit. )9>ai..i$) ^yy/JH*?iSoi*vy<gA*IF PYtl'tt OB ptt ftco |0A iHt OT Atv. STS WA S-lt'K-l FottlTiepBIY <l| SW.fTA^l rooliajor qevtOB*nv;f-eA^T ISSUED tbH APPft&VXV EakarK A m ca ent lH 640M0H--6VJULIT gffsy BECHTEL .CORPORATION SAN IXANCISCO THE TEXAS COMPANY PUCET SOUND WOKKS PROCESS PIP1H0 & iWSrftUMftWT OIAORAM RECOVERY SECTION CATALYIIC DOLYMtRltATION WT ww% ______ ht 2525 5"R A~5 m MXotJAO 5HSlRU^Jt?4T *TtAM nuttvm Ckcxxs asnotbd iiDpiic lMl; rCM^t TvIhOw-JNi) 3lo3p-LuI c4p-t*Xi-.C(H` fc`o AA . ! fc^,Z7-77 DR%emVI.cDn SrAA.tOS cpR-er CrVo-IrArwino .1 %J I REVISED PER ORAWIMS Tt %t[ [*1 ' *<* j :m none >wik J *. l cipwto ~' "" " BECHTEL S' TEXACO INC. PUOIT LOUKD SLANT m PROCESS PIPING INST. DIAGRAM RECOVERY SECTION CATALYTIC POLMERIZATION UNIT Worm - tcos TIUMBI' SPI9 `T` 5-RA-5 LITY LEGEND R-OILY WATER STEAM ?-SERVICE I I NOTES, SUFFIXES FOR INSULATION :d as follows; TOIEt protection CONSERVATION AL HEAT CONSERVATION HEAT CONSERVATION TINS TEMPERATURE CONTROL l TRACED a INSULATED iULATION WISE SPECIFIED. THE VALVE ALL BE BY THE CONTRACTOR is J-ID, PARA.513 FOR' LOSOPHY WITB REGARDS BE SUPPLIED BY THE "ARTICULAR .ATTENTION EN TO THE MODIFICATION WHICH COVERS SHUTDOWN F-FOR becht el - \ooys TEXACO EST. 351o 5tm&<>ls EXISTING ' NEW remove RELOCATE NOT USED-DP HOT REMOVE DEMOTES TI6-1H MUM&tks 2k MOTES I, REVISION OF MAJOR SYSTEMS ARE DESIGNATED bfi the symbols shown above, minor. REVISIONS ARE CIRCLED ANO INCLUDE A TRIANGULAR REVISION MARK, z. piping sEavite specifications for new LINES ARE IN ACCORoAMCE WITH &6MS J-SIDfl, TABLE 7. 3. LINE NUMBER 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 JHO IR$U_LATlltT^ 4 5TSAL5 SYWSS-S! !3J- Ta.eo V IthI- LINE IDENTtFICATION Ijl - 0-13J-6 -J13A- Nl T TTEXACOdJ-I ~ TEXACO 1 SIZE T ------ INSULATION REQUIREMENTS !P1ANT NUMBER SERVICE SVMBOl NUMBER 1TEXACO PIPING MATERIAL SERVICE SPECIFICATION 2k 4: v5 . /SL.L, '? 'X/Llofy'- 4DTICC InOoINtJH**CttZCCV(HlPrU>QINHRTCMDHttCMAROHCtlOlDWMTAEnMMPDfpMtOtAaKANXNOrOTIMa'0FAO#MNaTWJEVAITAflDOCW*O* I'MH|AVCBMDttMoUrttDCA.TILOHOItTtTtAotMu*MnHvA(iWe*LIINH7O0tRROloMAr OIDHMCOIIAFCTWANIAMT* URN TNIf OMAvrme NAOHPftr VfOH "JOUttr. ACO INC. 1G DEPARTMENT TON. TCXAS >)G FLOW DIAGRAM ARATIOH SECTION 'MERIZATION IJNIT - NONE tn*9*tQHtO no ntcono tmtntti OAT* 1 - 21 -72 5-RA-25 Tl.--v <iW E,p.= i.l,,,, S3 ii~----- STsa.n\ c. ' ' TctoC<%& &nw&OL5 A5 -SOTftD % A FL6S r> P-UisNu5t:*ri3*u5`Q'Z`oFpRpri ^s-CtJa.X. A .RGVHliO PCR. Pvi4 5.AA tlS- ftg.v. tA REVISED PER DRAWING 5'AArl25 REV.Q 2k *02 CCWTfc-jtTiON A % asfflaBHagsSaa " PTty''& ?? ist H .SEME NCVa | 0ES1QHEP BECHTEL [texa^ TEXACO INC. [texacI PUGET SOUND *LANT PROCESS RPING & INSTRUMENT DIAGRAM SAT FEED PREPARATION SECTION CATALYTIC POLYMERIZATION UNI" UtHtCL- 10095 TttttOMt- 3910 5-RA-25 7A WA-TEX 000403 \ ft ( 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 WA-TEX 000409 10.3 EXCHANGERS WA-TEX 000410 ` ,, : -f? *-\ r i- % - vj.v; ' U0>3> EXCHANGER- SUMMARY SHEET - CA"TALYTICiPOlLYMlER 1ZATI WTA. No. 1 Passes Diam. Inches , >' ^ .-V.` ;________ 1 ____________ DESIGN * V . >, "~ Shell Data _ Shell Tube Ha terial No. ` x Press Temp Press Passes S1G_ m t 4V.V. .*/.*#.: * * ' i - . .. . ' . i-. | } 2 2 i. 6 15-1/4 12 19-1/4 c.s. 1 : 650 c.s. 1 400 c.s. 1 650 300 650 65 200 300 300 300 275 150 i.: ' v \\..v ' * v! ; % f*c , . * *V ' * i# v . . *T. 1 "' -1 V " :' /. i EXCHANGER SPECIFICATION SHEET S CUSTOMER AND R PROJECT LOCATION TtENA^CO \4C. B plant Pu^e-r Sound exchanger no. ST-- C&& 1 SERVICE OF UNIT ProPKNX STaiPPtft SIZE t 2. * 7 *2. TYPE AEU . CONNECTED IN EXCHANGER MFB. Huc.HC.S- /^NOlS,OhJ R_eo. no. -2. item no \3 - - - .... SERIES PARALLEL SURFACE PER UNIT 35 +*' SHELLS PER UNIT |' SURFACE PER SHELL Qg ^ PERFORMANCE OF ONE UNIT 7 i FLUID circulated 8 TOTAL FLUID ENTERING 9 VAPOR 10 LIQUID LBStoR SHELL SIDE SraAiM 555 TUBE SIDE 5-m,n=.t3CR Bthsi 9<bOO 9<oOO 11 STEAM 555 12 non-condensibles 13 4 FLUID VAPORIZED -OR- BOWOeNSEB 14 j STEAM CONOENSED 13 } GRAVITY-LIQUID 16 J VISCOSITY-LIQUID C.p 17 3 MOLECULAR WEIGHT-VAPORS 18 {( SPECIFIC HEAf-UOUIDS 19 UftfeNT heat-vapors 5&5 352 S B.T.U./W . T. U./l* O. 4-<i 0.009(.W^k - O.O^fOor) 4-3.3 eru/x 8TU/# ^temperature in K TEMPERATURE OUT Fj OPERATING PRESSURE j NUMBER OF PASSES PSI 1 VELOCITY B PRESSURE DROP 4LL0w/cALG. 25 251 35____ 1 1. O / C> *f *f ft. /sec. * /SO.IN. H2 \\Q> 23 S 2 0-5 / O.S ^. FT /sec j*/so. in. y FOULING RESISTANCE MIN. 0.0005 0.001 HEAT EXCHANGED - BT.U./HR TRANSFER RATE- SERVICE 54-Oj OOP 35.1 CLEAN M T.D. (CORRECTED) I<b2 ACTUAL FOULING FACTOR C 0 NST RUCT.I ON DESIGN PRESSURE TEST PRESSURE CoS too */SQ.IN. <r/S0.1X. 27 S 4-15 */ SO IN */SQ IN DESIGN TEMPERATURE TUBES CKR&OH NO. &Q .SHCLL Cm^sqm Steel 1ELL COVER CAgfcoM STEEL. iS^fcoksaatIE*GTH _I2______ o. 0. ^ _II3L-I* VTHLIiC^yKANtErSS FLOATWIC MA0 COVER 2PQITCgH_ t CHANNEL -Qa S5U CHAWWEL COVER CAgeOtA ^>TCCL- .~TUBE SHEETS - STATIONARY C.AHB.QL1 g,TEEE .FLOATING BAFFLES - CROSS .Typt^^lHglJiTAsA,_THicj(NESs BAFFLE - LONG TYPE THICKNESS TUBE SUPPORTS THICKNESS gASKETS___ frUKT*^ JACKETSOi_JK>ag.5T<^SL CONNECriONS-SHELL- tN 9" oOUuTr I* -CHANNEL-IN OUT. ItATme ISQ*RF bat ms aoopy 44 H CORROSION ALLOWANCE -SHELL SlOE 45 CODE REQUIREMENTS ASMe tTnUaBcE tStliOitEr V1U PI TEMA CLASS kiA SPEC, 51M7 46 WEIGHTS - EACH SHELL BUNDLE FULL OF WATER 47 NOTE INDICATE AFTER EACH FART WHETHER STRESS RELIEVED tS.N.I AND WHETHER RADIOGRAPHED IX-R) 48 REMARKS . is 51 0P .A. OAT SA cc A Issus.o tafestD..For.^o'^vp.. Po*cwa.4._______ TV tf* .. JOB' NO. 100^5 m DRWG. NO. Ox OS-^fe-3 REV. 1 FORM H. 138 PART B 9 /6 8 WA-TEX 000412 i EXCHANGER SPECIFICATION SHEET CUSTOMER AND I PROJECT LOCATION Tex^CQ. StACc__ PLANT PuhtT Sound, EXCHANGER MEN. 5o*CWV___ mo- no. c^-oa EXCHANGER NO. ST>ClT ITEM NO 4 service OF UNIT DEPBopxMittRFEEQ Bottom Ey.OHA.h4C.ew 5 size' (g___x 24-O__________ type AES_______________ connected inseries PARALLEL 6 SURFACE PER UNIT 4-73 EFF. SHELLS PER UNIT SURFACE PER SHELL 4-73 EFF 4. PERFORMANCE OF ONE UNIT 7 FLUID circulated __ 8 TOTAL FLUID ENTERING 9 VAPOR SHELL SIDE oeppopANieew. ETesp_ L#*/tW 55 a 357. TUBE SIDE Qg.PROPft^Nr2.E.g. Btms. 4-^,ZS7 10 LIQUID _5.5,3ST 43> V*l.. II steam <2 NON-CONOENSIBLES 13 FLUID VAPORIZED OR CONDENSED 14 STEAM' CONDENSED 5 gravity-liquid 16 VISCOSITY -U0U1D 17 MOl fCULAR WEIGHT-__ Cp Q.&4-tUa1 - Q.4-9<o COot) Q. \4- Hsi) ~ 0-1 COot> 55.fe Q.4-53C lH)-O.SI4-too-r> oTofe C\>h V^oTuTootT 5SU.T te SPECIFIC HEAT-LIQUIDS B.T.U./W !Iu/ 19 LATENT heat -vapors B.T.U/W 8 TU /* 20 TEMPERATURE, IN 21 TEMPERATURE _ OUT_____ 22 OPERATING* PRESSURE psio JLQQjts: f Z\B IS4z$s 23 NUM BER OF PASSES 24 VELOCITY X FT. /sec. FT./SEC Jf IPPRREESSSSURE DROP 26 FOULING RESISTANCE 27 allow/caic. >z ..QjfiftX 4 /SO,IN. 1.5 / 1.5 0.001 f/so.in 23 HEAT EXCHANGEP-BTU./HR 1 , &BO.OOO M T.O. (CORRECTED) 4- Co 29 TRANSFER RATE- SERVICE clean ACTUAL FOULINC- FACTOR , 30 1 31 ! 32 33 34 35 36 TEST PRESSURE DESIGN TEMPERATURE TuBEsC>.uao4 Steel -I**- 5il?_L LC.AWCQM STU^U SHELL COVER CAftWOH ^TEEL CHANNE^g. CONSTRUCT ION 300 F/SO.IN. A59, /SO. IN. 300 / sa m /SO IN m Q-^yA." ***:3Ar-gjg LCW6TH a 4.0* PITCH 1 4J(S O 0. fcft IS `/A.1 THICKNESS FLOATING HEAP COVER QlNP^A^fcA Sff fH CHANNEL COVER CXftGHPW *- 37 iy.eE SHEETS - STATIONARY Carbon Steelfloating C^RBOH StCCA, 38 BAFFLES - CROSS CARaQK)STtE.L TYPE RIGKNESS 39 BAFFLE - LONG TYPE' THICKNESS 40 ! TUBE SUPPORTS THICKNESS 41 GASKETS W\^T>iV 7ACK6TEP As&I^TQS. 42 CONNECTIONS ^- SSHHEELLLL--IINN -3L" OUT *.* RATING 500* RF 43 -CHANNEL-IN OUT RATING SOP* RF 44 CORROSION ALLOWANCE -SHELL SIOE TUBE SIDE 45 CODE REQUIREMENTS ASHE SE-CTtOH VUIPlTCNA CLASS --sr SPEC. gm-7 46 WEIGHTS - EACH SHELL UNDLE FULL OF WATER 47 NOTE 'INDICATE AFTER EACH PART WHETHER STRESS RELIEVED (S.R.) AND WHETHER RADIOGRAPHED ( X-R.) 48 R S.M.$ Ms - BavCitlr Spacing 5 . Baffle Cut 33%_ . "S' .91 m ' w .A^iV**^ij.3tgE.V15CO> lw<pfiw. Cwnyr. fy m ATWfejuED Fp PgpcHAsfig SSZ SJOB-NO. RWG. NO. I REV. 100^5 os-5-6-1L: 1U WA-TEX 000413 t EXCHANGER SPECIFICATION SHEET w> 4 S 6 7 8 9 10 11 (2 13 14 IS 16 17 18 19 20 21 22 O' 26 27 28 29 , 30 ' 31 ' 32 ; 33 : 34 : 35 36 37 38 39 40 41 42 43 44 45 46 47 -4 CUSTOMER AND .. PROJE_CT_ LOCATION____ TEXACO INC, PLANT ______ E>oe.c.-rl GiUHO exchanger no. ,5T>.Bfefr. exchanger REW. HO. E.-0,&_____________ ITEM NO s.tRV!cA F unit Dc.pRQPAsHl'iLg.fL &QTT9M& CtOQlAR. size 19 * 24-0__________ SURFACE PER UNIT - 74S fype AE5_________connected in EFT. *4-. SHELLS PER UNIT I SERIES SURFACE PER SHELL PARALLEL 74S EFF <nfc PERFORMANCE OF ONE .UNIT FLUID TOTAL CIRCULATED ___ FLUID ENTERING VAPOR SHELL SIOE t)6J=>ROPA>4txPt BtMS ih!m 4S>AS-X TUBE SIDE Coomhc, Water -F3j OOP LIQUID STEAM 4-9>>..g57. 7S,.c>^P. NON-CONDENSIBLES FLUID VAPORIZED Ofl CONDENSED STEAM CONDENSED GRAVITY-LIQUID Sp VISCOSITY - LIQUID -<=E_ MOLECULAR WEIGHT-VAPORS SPECIFIC HEAT- LIQUIDS_____" LATENT HEAT -VAPORS 0.514- (Im^- 655A^ouy^ O-n nK.V~Q.4-SCQ^TT B.T.U./* b.t.u./# B T.U /* 7t u /* temperature in temperature out operating pressure PSlS HUM BER OF PASSES VELOCITY PRESSURE DROP ALLOw7c*L6. tS.4. loo .2^9 4-/4- *F FT. /SEC. 4* /M.IN. 16> IOO 4-0 & 4- 12 / 12 FT,/sec -P/SO.IN. FOULING RESISTANCE 0.001 0-005 HEAT EXCHANGED-BTU./HR TRANSFER RATE- SERVICE DESIGN PRESSURE U7SO.OOO________________________M T.O. IGORRECTEP) 2,3. B Tfe.S___________________ CLEAN_________________ ACTUAL FOULIHS FACTOR CON S T R U C T I 0 N 300 */S0.IN. ISO */ SO.IN. TEST pressure DESIGN TEMPERATURE TUBES lUH kOM NO. 195 shell Ckraom Steel 4-50 */ao. in. G50 F 0.0.3/4 BWS.IC* !ft LENGTH 1. D. -. 19 >/A THICKNESS 225 fo5 240^ PITCH 1" */S0 IN *F 4t O SHELL COVER CARBON &TCEL channel Ckrum Steel FLOATING head cover carbon Steel CHANNEL cover CAvtt&oU Stslel TUBE SHEETS-STATIONARY NK>/4U ROLLED * FLOATING UKVA.W 2ll.R& baffles^cross CARB4h>,STC.gU BAFFLE - LONS______________________________ TYPt_______________________ THICKNESS TUBE SUPPORTS _________ THICKNESS gs-KETs . Mg-TKV 3~AsCKgTC.O CONNECTIONS-SHELL- IN 4 -CHANNEL-IN 4 CORROSION ALLOWANCE-SHELL SIDE OUT OUT t/fl* te>4 ___________________________________________ 4 RATING ^QO Rf RATING ) 5O ffF ..................... TUNE SIOE I/ft* CODE REQUIREMENTS A&Mg GtCTIOH V>U Q>TEMA CLASS R WEIGHTS -- EACH SHELL lUNDLE FULL OF WATER SPEC. g-tM1 '~ MOTE INDICATE AFTER EACH PART WHETHER STRESS RELIEVED IS.R.1 AHO WHETHER RAOIOSRAphED <X-R) g.^RKsbaffle 5" . a^gue *mt IQ...... ........... . ---- 51 0 REV. 0*Tt tAh. EVI4*.Ov feSOEO 'fin* CaWST pe tJOB NO. ORWG. NO. REV. (Jt fa 10095 ` &S-S-C-2 1 WA-TEX 000414 10.4 PUMPS WA-TEX 000415 TABLE 10.4-1 JGAL PUMP SUMMARY SHEET Polymerization unit plant,sa lACORTES. WASHINGTON DRIVER DATA Fun Rated RPM H,P. , Load Type,_ Amgs 3600 15 Motor %f I e* 3. u I' '* WA-TEX 000416 2- I i 1 4 I r~~'\ .r % in u NO 130 (REVISED APRIL E ll CENTRIFUGAL PUMP DATA SHEET APPLICABLE TO: PROPOSALS O PURCHASE^ AStUllTO NOTE. < ^INDICATES INHUMATION TO K COMPUTED RV PURCHASER; BY MANUFACTURER E.X ISXVV1G. VbMP JOB NO.LQ02>S-JTEW H0.J5.3. - _______ PURCHASE ORCER NO-l -O *?S. REOtXMTMNNO..LSSPlS * mmm.____ . . DATI-l-l.. . REVISION .Cat, - O'S- FOR rrit'LiKi.O, Imc. UNIT Ch-r. PQLy MlftJMKMQtt. -NO. MOTORS REDDJb=-ITEMMJS5=^M^ SITE____ PROVIDED MrluUdBfXC^MTDW... NaTmw*M*KrD_rr____ item no.___ =_____ provided by. tump mfr-Wlt-SbKi - ____________ sfandtype-I fa.A.'Lz r-______ mtdby_ --. .... .sbraino._ PERFORMANCE /<\ -13.0- iWLTQU1D--Ji&fAUS'IL------------U.S. 6PM at IT. NOR- RATED- PT.f.NOR._fitCL_MAX._ SP ERUPT t.D VAP PRESS. M pT. P3A_ - BISCH. PRESS, PSM-SUCT.PRESS.PStB MAI -DIFF. PRESS-PM_____ -WFf.HEAO.fr________ _3fil -RATH)- JLSL M VI&ttPT.Sw_________ _CP_ CORR/EROS. CAUSED BY-- -NPSHA.PT___________ -HTD. HP- rLrt-,C> 4- PROPOSAL CURVE N0._3b-l.5fc3O>.. RPM 3550 HPSHR (WATER)JLiifep-. EFF.____EJJ____ RHP RATED L|g.^ MAX. RHP RATED MP 505fft MAX. HUD Mitt IMP MM. CONTINUOUS SPM ROTATION IV1EWE0 FROM CPL6 END)_ ECONSTRUCTION SHOP TESTS NOZZLES SIZE RATIRt FACING SUCTION 100 RF DISCHARGE _____tii.. -a&p.-. RF CASE-MOUNT. CENTERLINE DEOOT RACKET VERT.(TTPE)- SPLIT- D AXIAL DRAB: TYPE VOLUTE SOL DRRL WPH1SIR PRESS: OMAX. ALLOW.PSKF: D HYDRO TEST- LOCATION TOP TOP ___ PS Owit. pew. ONON-WIT HYDRO OWIT HYDRO ONPSNREOO OWT NPSN OSHOP INSPECTION Oogmant. t hmp. after test OOTHU. - . . -CONNECT: DVENT FRAtN DBA6E . .. . IMPEUER OIA,, RATED_____ ______ ? " (OS. PMAX_____ /.Ufa--- /S\ TTPfcCLflSEftffl MATERIALS MOUNT: BETWEEN IRES DVBDWHB BEARtNGS-TYPE: DRAWAt= THRUST WEAR RB. OML/CIRNC---------------------------------- API CASf/TWM ClASSO-iaEi3S^JEs2.H.1 LUBE: OBINS OIL 0(1000 OOILMIST DFIRMER PRESSURE J&BfeUT-JLA3 COUPLING: OMRFOmm. DRIVER HALF MTO RY: OPUMRMFR OMIVERMFR ORURCNASER gK&lr ^Cr IVUaFT- Utuo -UT. PACXING: MEN t TYPE . : S!H/NO.OFRt6S_ MICH. SEAL: DMFRR MODELAPtClAtS.COM___________________________________ MFROCOE- BASEPLATE. VERTICAL PUMPS AUXILIARY PIPING O CW. PIPE PUN- .OCU; Oil: OTUMND: OPIPE- O TOTAL COOUNC WATER REOD.SPM- .OSHHTPl RECTO- OpACKINS COOllNe HUfCTKXY RECTO: DTOTAL SPM DPSS OSEAL FLUSH PIPE PLAN.__________OCA OKS. OTUMM ONPE- OEXTERNAl SEAL FLUSH FLUID OBPM________________________________ Oalboliary SEAL PLAN Otl OSS. OTOWNS OP*t- OAUX. SEAL QUENCH FLUID- HP__ _ MFR- . TYPEINC OVHS OVSS, MOTOR DRIVSR -FMMC- -vero/PMSE/naB- .lEAMNSS- -LUSS- -MSUS- -fULLLSABAMPS- __ TEMP MSEC________ -LOCKED ROTOR AMPS- VERT.THRWTCAP.il. . ItWICE FACTOR- PSW- rrTORSUMPOBTHO__ MHA SURMEN6INCE REO'D.n-------------------- ---- COLUMN PIPE O FLANGED OTHREADED LINE SHAFT: DOPEN ENCLOSED MSS: DROWl_______UNESHAn... . MM LURE DWATER DOIl DGREASE FLOATS ROB OtS. OS.S. OBRZ ON0NE Float switch a------------------------------------ POMP THRUST, LB OUP- . OOWN- APPROX.WT. PUMPS RASE___________ MOTORTURWNS- API5TAHDAR0 SI080VERN8WHEttOTHERWISEHCTFO C-XSTSTV v\0. Pq.|Ag.,,,M.Tx0.lFVMa-^St- MEiCftl S Sgg\itc<; - Maws IjLP>et.L.ieA4 Na3 g &ir. rCikSfi fc--------------------- I'Ut-n1 lAlVl?1r> FOfJL F>\jRt.KV<Lt3 O )^ui?n for ounTATiotM NO. DATE JOB HO. DRAWING NO. REV. V* 4 ti r* & fa IP09S SHEET DS-S"6-i I iJ .OF----- ---------- WA-TEX 000417 ( CENTRIFUGAL PUMP DATA SHEET O O OAPPLICABLE TO: PROPOSALS PURCHASE AS BUILT BOTE. < J INDICATES INFORMATION Tp IE COMPLETED BY PURCHASER: ey MANUFACTURER JOB M./0O9S ITEM NO.. SkT- PURCHASE ORDER NO._______ ________ __ RBJimta. lOQ3/5T _____ ___________ DATEREVISION............... fob 'raw* UNIT .. --CtATA t'fXlC-P,--bL-^--M---e--t-U- -Z--A---X---t-Q---t-l-.------ SERVUE F&bo SyPkss 2NO. PUMPS REP O _>? NO. MOTOR* RED'D- "X ITEM NQ.g'J- G& /A PROVIDED KtjfStM/ZM&Cjm B fit V NOTUBtMES RHrn ----- ITHtHO ----- PROylpiDBY________ __MTDBY_ . PUMP w*.3. Sin AMO TYPE //VF X 27/Q'&/sS3sinxi NO ... OPERATING CONDlTIONt, EACH PUMP LIQUID. C.3/C4. I -US SPM *tPT. Wm.__^L_RATIB_ -BSCH. mss, rsm__3 S7.. PT. F.NOR^aQ_MAX. SUCT.PRESS.PSIGMAX, ?,?<?------ RATER. Qj.475. 7-7-SP GR.M PT. ---------- Bff.FRESS.FSt_____________ VAP. PRESS HFI.rM-.Z37___ Bff.HEAO. FT. VIS. t PT. SmCPj^LPSHA. FT. CORR/EAOS CAUSED BV________________________ _HYftHP_ CONSTRUCTION PERFORMANCE PROPOSAL CURVE NO. mtJt&S&msm iwa7eb)_JS. &CLEff. vay?g ,HP RATED, MAX. OOP RATED IMP___ MAX. HEAD BATH) IMP-- -&GQ . / SL____MIN. CONTINUOUS 6PM. j . ROTATION (VIEWED FROM CF1G END). gC tV SHOP TESTS MOZZLES sin HARM FACING SUCTION 2........ s3oo* DISCHARGE zmz. /?/= CASE-MOUNT:^CENTERLINE DPOOT BRACKET VERT. (TYPE). SPUT: O AXIAL JflflAO: TYPE VOLUTE PRESS: nut* tnnm Fpl^>7 * DDL DDIFFUSER F OHYDRO LOCATION 7~0& .-JjQG.rSK ONON-WIT HYDRO OWlT. PEfiF. $W1T. HTDRO OKPSH REDD. OWIT. NPSH g$HCP INSPECTION OOtSMANT. A MSP. AFTER TEST OOTNER........................... *frgT n--CONNECT: INVENT ^ERJIN lASE _ OTtr&aLZSGnb IMPELLER OIA- QRATED. MATERIALS MOUNT: BETWEEN MGS !RtftM6 was RS. OtAM/ClRNC- BFARINGS-TTPE qradial. &CJ2*__ othrustA^ LUBE DRING (ML FLOOD QOIL MIST p&IHSEA OPRESSURE U7A API CASE/TNM ClASSO_______________ &JZMS_____e--2M77- COUPLING: PMHF MODEL____ Q. &GM3___ -jZA-L. DRIVER HALF MTD BY: JSJPOMPMFR ODRIVERMFR O PURCHASER PACKING: niAFRATYPE DSUJ/NO.OfBNE MECH. SEAL: MEN A MODEL L^P-^A<!r CP^3...AP1CI. -.. MFRntnc G>/B~ 2/; BASEPLATE: VERTICAL PUMPS AUXILIARY PIPING OCLW. PIPE PLAN____ TM___OCU: OS.S.; OTUMND: OWE------------------- TOTAL COOLING WATER RED'D. SPM G__________ OMBNT F.I.REOrD_ OPACVmS COOLING INJECTION RIOT* TOTAL 8PM DPStS OSEAl HUSH WE him /CP ]Krg OtS. OTOOWG )jfptfsi OtXTERNAL SEAL PLUSH RUID OGPM. PS16_ OAUXB.IARY SEAL PLANOCS QS.S. OTUBING OPPE.0AUX.SEALOUENCHBHHi U> trtt. Q.tyfUfcM CoA* AJ. f?Efcg_ MOTOR ORIVIR .voir_________________ .LUBE, <5>p3T TYPE. jhftS>.4Z/,7L JN...S._U_l_-_ FULL LOAD AMPS. HC TtSSC-TatR RISE. C<S2_10C0 ROTO* AMPS. OVHS OVSS VERT. THRUST CAP.El. . SERVICE FACTOR. PIT0RS0MPDEPTNO________________________ MM.SUBMERGBKE REQ'D.O------ ------ --------- COLUMN PIPE FLAN6ED THREADED LINE SHAFT: DDPEN Q ENCLOSED IB6S: PBOWL DUNE SHIFT BAS. LUBE DWATEN OOIL DGREASE BOAT A BOD OC.S. OS.S. OBRZ ON0HE FLOAT SWITCH ------------------------------------------- POMP THRUST. LB UP. .DOWN- APPROX. WT.PLWA BASE. MnrtlB '2J5'2- .TURBINE. API STANDARD *10 GOVERNS UNLESS OfflOVRSE NOTEtL. FORM NO 1)0 (REVISED APRIL 71| 1# 1VW7? 0 NO. OATE jaaie. .j&tfrG&A&B Can OuoTfcTiOw SL job no: DRAWING NO. REV. fOC&S 05 \ SHEET ./ .. .OF...U WA-TEX 000418 ( WA-TEX 000419 m t I WA-TEX 000420 f 1 WA-TEX 000421 t 10*5 INSTRUMENTS WA-TEX 000422  * -1/Sjf. .-. . ` < ' Flow Element No. ' 5FE-19 '5FE-200 5FE-201 5FE-205 5FE-206 5FE.-207 SFE-208 ' ' ` ,'jp 'S-S-s- i Y FLOW ELEMENT. SUMMARY' SHEET v r' ' i,*"*'. . *? ..............i4>*> v' : CATALYTIC POLYMERIZATION UNITPLANT SJ * *> ' vl :^ s%. ANACORTES.. WASHINGTON. Service f..* -' . V*. >> '.; - *" `:V a -; , Orifice Sl2e Line Size Meter Coefficient Btms. Cooler Outlet Amine to 5J-C57 . Caus tic to 5J-C59 Deprop. Feed Bypass Stm. to 5J-E58 Deprop. Reflux Stripper Vapor Outlet 2.132 . 8'*` / . , ( 1-978 1.238 1.123 1-959 0.901 1.923 3" Sch *t0 3" Sch 40 2" .Sch 40 2'-' Sch 40 3" Sch 40 2" Sch 40 3" Sch 40 40 BPH 15'BPH 8iBPH 8 BPH 100#/Hr 4 BPH 4000 SCFH fgi * V 1 t i 3 .2 WA-TEX 000423 * +* i;\V''-?"'J'''. . *">,. -%3u- Tag No/ 5PSV-10I 5PSV-102 5PSV-I03 5PSV-104 5PSV-105 5PSV-I07 5PSV-220 " *' Service .. " 5J-C57 5J-C58" . 5J-C59 5J-C60 5J-C61 y'J-BSi > 5J-E58 TABLE 10.5-2 RELIEF VALVE SUMMARY SHEET CATALYTIC POLYMERtZATt'Oli UNIT PUNT 5J iMcUIURTfltl Size 2*' X 3" .1 t< . it V 1-1/2" x 2" 3/4" x 1" 1-1/2" x 3" --Set P.ess' 310 PSIG -," ii it 260 PSIG 75 PSIG 65 PSIG WA-TEX 000424 f