Document G5ZayBDE9wDREJonXLNywNg3m

ADDENDUM TO OPERATING MANUAL GAS RECOVERY UNIT PLANT 4B TEXACO INC. PUGET SOUND PLANT ESTIMATE 3910 BECHTEL INCORPORATED HOUSTON, TEXAS 1973 j WA-TEX 000754 ) WA-TEX 000755 I TABLE OF CONTENTS 1. General Description A. Introduction B. Basis of Design General C. Description of Additions and Modifications Compression and Absorption Section Distillation and Treating Section Uti1ities 2. Control Features A. Principal Control Features 3. Preparations for Startup A. Startup Procedure 5. Operating Variables 6. Shutting Down Procedure 7. Appendix 7*1 Process and Utility Diagrams 7.2 Vessel Drawings 7.3 Heat Exchangers 7.4 Pump Data and Curves 7-5 Instrument Data 7.6 Tray Loading Data Page No. 1 1 1 1 1 2 2 2 k k 5 6 8 9 WA-TEX 000756 WA-TEX 000757 ( I - GENERAL DESCRIPTION A. INTRODUCTION This addendum to the Operating Manual for the Gas Recovery Unit at the Puget Sound Works of TEXACO Inc. at Anacortes, Washington, covers the revamp of the Gas Recovery Unit. The major revisions to the Gas Recovery Unit are: New and modified heat exchangers Replaced and modified pumps New trays in the Debutanizer Change of service for caustic treaters Revision of piping B. BASIS OF DESIGN General The FCC Gas Recovery Unit is to process 15,000 BPSD of FCC fractionator overhead liquid and 20 MMSCFD of FCC fractionator overhead vapor. A small C2-C3 stream from the Alkylation Unit is recycled to this unit. The FCC Gas Recovery Unit recovers a C3-C4 stream and light and heavy FCC gasolines. The C3-C4 stream flows to the treating section of the Cat Poly Unit. The light FCC gasoline is caustic-treated and directed to storage. The heavy FCC gasoline will, normally, flow hot to the hydrotreater unit, or will be cooled for storage. In either case, the existing caustic treater is bypassed. The heavy FCC gasoline may also be cooled and caustic-treated for storage. A fuel gas stream is recovered from the sponge column. Process flow conditions for the revamped Gas Recovery Unit are shown on the revised process flow diagrams, IhRA-1 and it-RA-2. C. DESCRIPTION OF ADDITIONS AND MODIFICATIONS TO THE UNIT This section describes only additions and significant modifications to the FCC Gas Recovery Unit. Reference should be made to the Operating Manual for the Gas Recovery Unit for a description of the existing facil ities. : WA-TEX 000758 I Compression and Absorption Section (Ref. PslD's 4-RA-6 and 4--RA-7) A new line is added from upstream of the absorpti-n-oi1 cooler, 4B-E3, to upstream of the second stage separator, 4B-C7- The'purpose of this line is to permit reduction of the liquid loading in the absorption section of the absorber-deethanizer, 4B-C1, if necessary. The absorber-deethanizer intercoolers, 4B-E6 and 4B-E7, and their circu lating pumps, 4B-G7 and 4B-G8, have been taken out of service. The absorber-deethanizer second intercooler, 4B-E7, is re-used as the light FCC gasoline trim cooler. Distillation and Treating Section (Reference P&ID 4-RA-8) New trays are installed in the Debutanizer, 4B-C3. A new splitter re boiler, 4B-E51, is added in series with the existing splitter reboiler, 4B-E13. Reboil heat to the new reboiler is supplied by circulating hot slurry o'il from the FCC fractionator. Feed to the splitter, 4B-C4, is preheated in the new splitter feed-bottom exchanger, 4B-E50. Heavy FCC gasoline from the splitter feed-bottom exchanger, 4B-E50, may be sent directly to the hydrotreater; may be cooled in the heavy FCC gasoline cooler, 4B-E14, and the heavy FCC gasoline after cooler, 4B-E18, and sent to storage; or may be cooled in the heavy FCC gasoline cooler, 4B-E14, and the heavy FCC gasoline aftercooler, 4B-E18, treated in the heavy FCC gasoline caustic settler, 4B-C11, and sent to storage. Light FCC gasoline is cooled in the light FCC gasoline trim cooler, 4B-E7, treated in the light FCC gasoline settler, 4B-C12, further cooled in the light FCC gasoline aftercooler, 4B-E15, and sent to storage.. Uti 1 i ties Utility consumption by new or modified equipment is given in the table on the following page. 2 1 WA-TEX 000759 Item Number 250 psig steam 4B-GT9A 4B-GT11A AB-GT30A 1*B-GT50 GT50A Service Absorber-Deethanizer ReboMer Circulation Pump - Spare Debutanizer Product Pump - Spare Absorption Oil Charge Pump - Spare Splitter Column Reflux and Product Pump and Spare Consumption 5,186 #/Hr. 3,7*12 //Hr. 8,510 #/Hr. 3,322 #/Hr. Cooling Water *tB-E7 ' Light FCC Gasoline Cooler 1*1k GPM Electrical *1B-G9 *1B-G11 Absorber-Deethanizer Reboiler Circulation Pump Debutanizer Product Pump *17.2 BHP 51 BHP 3 WA-TEX 000760 | 2. CONTROL FEATURES ~! , ;S* WA-TEX 000761 i II - CONTROL FEATURES A. PRINCIPAL CONTROL FEATURES The principal control features are not changed by this revamp. Reference should be made to the Operating Manual for the Gas Recovery Unit for a description of the control features. The following control valve changes are made: 1. The existing 4FRC-11V is replaced witha new 4FV-11. 2. The existing 4FRC-11V is relocated to replace the existing 4FRC-29V. 3. The existing 4FRC-29V is relocated to replace the existing 4LIC-70V. 4. The existing 4LIC-70V is surplus. 5. The existing 4LV-34 is moved from downstream of the heavy FCC gaso line cooler, 4B-E14, to downstream of the feed bottoms exchanger, 4B-E50. This change is necessary so that level control can be main tained when heavy FCC gasoline is sent to hydrotreating. 4 ; WA-TEX 000762 ,, i-lw .tWJf* .*p 3. PREPARATION FOR OPERATION . WA-TEX 000763 I III - PREPARATIONS FOR STARTUP Reference should be made to the Operating Manual for the Gas Recovery Unit for a description of preparations for startup. Blinds should be Installed in the intercooler draw and return lines of the absorber-deethanizer column, 4B-C1. These lines will isolate the intercoolers and Intercooler circulation pumps that have been taken out of service. 5 < WA-TEX 000764 , -.-r-Hsit "T-" TTCfPn*- b. STARTUP PROCEDURE WA-TEX 000765 f IV - STARTUP PROCEDURE Reference should be made to the Operating Manual for the Gas-Recovery Unit for a description of the startup procedure. Startup of the revised unit is the same as the existing unit, except the new equipment is integrated into the startup procedure, and some intermediate and product streams are rerouted. Additions and changes to the startup procedure are discussed below. The following new or relocated exchangers are steam-purged, tightness-tested, and pressured with fuel gas in conjunction with existing equipment and lines: Exchanger Number Service 4B-E7 \ 4B-E50 Light FCC Gasoline Cooler Feed Bottoms Exchanger 4B-E51 Splitter Column Reboiler The following new lines are steam-purged, tightness-tested, and pressured with fuel gas in conjunction with existing equipment and lines: Line No. Service 4B-0-367-3" Absorption oil bypass to 4B-C7 4B-0-376-2" 4B-0-350-8" Rich sponge oil from 4B-C2 Splitter feed to 4B-E50 4B-0-351-8" Splitter feed from 4B-E50 4B-0-363-4" 4B-0-364-4" Slurry oil to 4B-E51 Slurry oil from 4B-E51 4B-0-365-12'* From 4B-E13 to 4B-E51 4B-0-366-12" 4B-0-352-4" From 4B-E13 to 4B-E51 Heavy FCC gasoline to 4B-E50 4B-0-353-4'* 4B-0-354-4" Heavy FCC gasoline from 4B-E50 Light FCC gasoline to 4B-E7 6 WA-TEX 000766 Line No. Service 4B-0-355-4" Light FCC gasoline from 4B-E7 4B-0-359-4" Heavy FCC gasoline to 4B-E18 4B-0-357-4" Light FCC gasoline to 4B-E15 4B-0-361-4" Heavy FCC gasoline to storage 4B-0-360-4" Heavy FCC gasoline to 4B-CI1 4B-0-362-1" Gum inhibitor to 4B-0-360-4" 4B-0-356-4" Light FCC gasoline to 4B-C12 Feed to the splitter column, 4B-C4, is routed through the feed bottoms exchanger, 4B-E50. The new splitter column reboiler, 4B-E51, is started up in parallel with the existing splitter column reboiler, 4B-E13- Splitter bottoms is routed through the feed bottoms exchanger, 4B-E50. Light FCC gasoline is routed through the light FCC gasoline cooler, 4B-E7, the light FCC gasoline caustic settler, 4B-C12, and the light FCC gasoline cooler, 4B-E15, to storage. Heavy FCC gasoline from the feed bottoms exchanger, 4B-E50, is routed directly to hydrotreating, or is routed through the heavy FCC gasoline cooler, 4B-E14, and the heavy FCC gasoline aftercooler, 4B-E18, to storage, or is routed through the heavy FCC gasoline cooler, 4B-E14, through the heavy FCC gasoline aftercooler, 4B-E18, and through the heavy FCC gasoline caustic settler, 4B-C11, to storage. 7 WA-TEX 000767 i WA-TEX 000768 { V - OPERATING VARIABLES Reference should be made to the Operating Manual for the Gas Recovery Unit for a description of the operating variables. Operating variables for the revised unit are the same as the operating variables for the existing unit. 8 j WA-TEX 000769 I [' 6. SBUTDoW j PROCEDURE WA-TEX 000770 ( VI - SHUTTING DOWN PROCEDURE Reference should be made to the Operating Manual for the Gas Recovery Unit for a description of the shutting down procedure. The shutting down procedure for the revised unit Is the same as the shutting down procedure for the existing uni t. 9 WA-TEX 000771 ( i 7. APPENDIX j ! WA-TEX 000772 I' 7. Appendix 7-1 Process and Utility Diagrams 7.2 Vessel Drawings 7.3 Heat Exchangers 7.h Pump Data and Curves 7.5 Instrument Data 7.6 Tray Loading Data WA-TEX 000773 I 7.1 PROCESS AND ? UTILITY DIAGRAMS [ j WA-TEX 000774 TABLE OF CONTENTS SECTION 7.1 PROCESS AND UTILITY DIAGRAMS Process Flow Diagram Process Flow Diagram \ PS ID PS I D PSID PS ID - Utility Utility Usage Diagram GRU - Compression and Absorption Section - GRU - Distillation and Treating Section GRU - Compression Section GRU - Absorption Section GRU - Distillation and Treating Section GRU - Gland Oil and Flushing Oil GRU l-RA-l 4-RA-2 4-RA-6 l|-RA-7 4-RA-8 . 4-RA-11 4-RA-25 WA-TEX 000775 Krr>tyinT) v l*" UMtt tteoo cm W* j ia 2aa ; y.O'p aaoTiwo ** t >'U u iO -' >t 6Ptb *WT ia 4LWJ .ft. Ttt -Hti tt . f-i' rtf IMS 1V>tl t/Mt OPU an `, V w Mia A,P&0 tWWA SL1M> CFM IUK r 7U>i 1*6 HXKH ammi --RICH Amur To*A AWJC tttlBttt tun. m - .RtatKCRATJOM-VMtL. IMM ieowtrwtg.tcc,re>ctroHCai 11 .............................*"*..' oainwanur lwnjjfn w mMfeziktcaxMuu^RMMiiiJi' lMOHoat'tmftwaxtJt amM* iMauvANUta ^<SS2 aunam.Tg gwnwtagagrJmw MC-b nxstuomiitJEvuTnt *-EJE5> 4i>>b ***&> . . REFERENCE DRAWINGS ft0ORFt0iUutUttcriM4t>M tttUftt tfcite*.P-CC-Uuir VtA-2 rctm>v>*cM%uiQitrtnsiMttr.. &\ niton** butt 4*1 NiAwwtc WKrca3VttmiHfcnoN,>tt.vHir 3-0* \I j \ ) } 6"' * Stea. m s-RoOeer *=2? DENOTES ' PIPtMO. EQUIPMENT * 1H5T.RUM6HTS AODtD OH C-UttO X hcvimo ret ctimatc 3*oc (U* TP & Aft Jtk w RtMOVtO HOT! t VSO *A St A mvsrcrowds stDM.+<Att tu * >.4 e* fCAUVfCt PKG.4-UL44 1 p *iA <v * *# nvt* cm coftSTROfne* .w**<*f Im AT k'r * A Wi KH.UVT or CM<fMteP*.4<A.|' y r A* % w isttrio f#t ArratvAL ir JW tot liwi1 ' , ' }***** HC-RtOCXHDlRM es IXCHTIt COmtAHOM tMHMKUCO ' DRAW1HO tTATVS * K* MTS KtCUt^Cw* -2 ^S/Tt H#t*M*vw*MM?* 1 V*V* ** A6P4W0/t0O ,,Jt&V - iMdlVU CO. : THE TEXAS COMPANY FViHfr fOCH wtxxs PROCESS flOW DIAGRAM COMPRESSION 4 ABSORPTION SECTION . GAS RECOVERY WK MWMMk wt. 2525 4-RA-l 6 i 5-R JOB KO.C-mtO DWG- NO. 22213 ` SHT. NOT.0+401 Ii WA-TEX 000776 t P* M I 3C*3R jolOt*ou S- TUOf(tArtf*tf|*T'A*M*fc NUlfc5. * CA4* 'A ts to* 6/ltiflOW W WICK 40 YQUIUI % 6+ in M 14 OllMlAlt PMftVCT. ** V I* t<3* ontAUOH trf WWCSt TO VOVUMfc % Of T* tfumt mo It OltTHUTt PRODUCT. a. 6MD 4*4*>T U) Ar OUkiXlUk tOUHUOK*. BdtrOHYpPTQuAASOtSiuvMqt&-txci *atcvm*AAcAf.ii&ctnr*jco>\v.uwtp+t*o1*i1g*%uocmjcaTt-Otkaiia*vtyiOihoPAipSmAOC^AoApfKuaAKutJte.iFAWstcotsftwtmtq*t.tOe.>aYt S, i >0 PftIC *.rtajjt ihs fc.01* OfM tW *^r" Hid tJT \ rttAVY tec (UIOi)Ml TO UtfWr >C6 OATPUm IP Cv c4 no tf%4 fttMOYAl 5WT CA04T)C 70 Pl*?Al 4> REFERENCE 0RA.WUJfiS PBoetbj now iAcm4.!turxtu?>6*ttt>i! ucl,t<cvn VlA PAQOISt ILM 0(k4IUA.^a<A|lV<m.4taibaUYtVrMift U>>) poocm now oii6*au.p, mip <(cr,eir.PovY uutr **vi^L dS2> L -i ,*g?4 >t>o# mjftcnoH 0l#G pump A V-Y" A $A A*! 'Mi * ikt <# row& teral nfi tot un w otuum *-u-vt j imp 10a coirmucTiaumuMU^ rot iw Ct tMl Ml 0*0 *# Jl *Mr. at * w AA. ** MUX* MX UfkOlli. > tu } j - * 5% IKW *04 ;|mmm |mmh )l'Cl< m ftSCHTU CORPORATION UMIVMtKO 640O--&____ THK TEXAS COMPANY . PUMT JOVMPWOMS <D PROCESS now DIAGRAM PIS7ULATI0H TRtWI>J(3 S6CT10H 6A RECOVERY UNIT 2525 4-M-Z WA.-TEX 000777 WCTHUmtf.TffT I ~1_T l SHCHCH RtataNM7tM I |MSLAT*M- - INSTRUMENT SYMBOLS ukuv Mouxrto ROATO MOUNTtD E TIUNRMiTTl* maaautcttc.c9WM CONTROL. Am UUK tkCCTfllCM. UAP cwllarv ntamo = -PLANT HVWRtA -IHtTAVMtMT tfiCMTlFtCATlON - IHiTOUMtHT MUMttA INSTRUMENT IDENTIFICATION ALL INOTKUUKMrt ARC CODED * ACCORDAjrCC WITH LS-i* STAMDAROA txctrr AO MOTEO OR RRMft TO CPA*4 MR BRUVSi ( LINE IDENTIFICATION \s W0T65 ECVl6t0N* 0F MAJOR. 5VDT6MD ARC OtitgjWATtD Y TUg WMOOwS fMOWH AfcOVC- UlNOR. EfcVl*t0N* ARE :%cl&0 AWOlNCUIOt A TRAxgUU4. CtVi^lOM pipino exvice specie catiohc fob. NEW UN&S Ate IM hCCoiQAHCt With QM> J-3DD TADkft 7. . L>t klUUfrEK. 4iiPix6 FOA ^U.ATl^N Aft* pgNTigtD AS FOLLOWS*. ev PtttSOMMtt . PROTfetriON CC COLO CON4&eVATI^H PARTIAL iAT COLSEftvATlON Full heat cou^eavATio^ \ CPCCAt(N6 7wFtRATURt CHTSOvj 5TCAM TRACED AMD >k.*SULATD / Ua CWSO.AtlDN ___ MMUO snCtfiCAIIOMtiMt &>it ,AMTMb8CMr|k - nmctxKeMv*M**| PIPING SPECIFICATION isoti.r.RAnt,c.i..rvc*R auj>wac CQttfR Cl y>QTC0R AllpWANH Toy*t.r. dATt. C>t. #*>*. ALyowAMCt >00*g..6PCKt. MUWANC* I S0*JLK QAUS.C.t.ji-'Cek*. AlLAwlAWCI HPRr, COCKS Ct-VfCMt. AUFWAWCt 100*1^C>tt. AllOWAMC* Hg*Ar.MmtTt>t*ATtt,C.t.CtM*UT Ll PL 5Qo*tc>c*jrES, yycotrx.RLLQvUKLis*. COMMODITY DESIGNATION HVft*SRR*ms,L>QUI VAM, RTlAv* 1CJHORH3M4. SI9VIC* WAT1R C0OLIM* WATtA *OU* WAT** ITEM NUMBERS LINE IDENTIFICATION I A -0-4. 'ixacoT rex*e tANf SERVK... NUMfiCR EYMSOLvi IS* ADDED \ , 4aST!3-3* J34-PHC. ADDED ^ . VAUVE CDDtf ^ 4C-6T30 ~~----------- ' y I i$k i. DEiirree iu-o-3 t. APDir-D TIC-IN l*B-*.<> *** 3. A,peD PgVAH r,tTt at i.o-5s/s.ft- la la TO AA5QAM.R OlfcTHmUtR COUIWM TO MtWIU PtETHANlZUt COLUMN **<l PCfcU 0>H.vOUID TO COOt 4Rt> SOUR *AI '>0 *UR SUC64 01UM S*C0 NOTES J. rtMA TO** FVftHllHt* Ay v**0 W)T** ALCDCtATl* >IC* OF MAAftft |QOlM*HT UARKtP *. T, DRAIH* ON H`CG AN&4XT T** lOC*T* At *' Vow oomr OF V*Ct*L OR VXCftC. CRCTtO*. y DRAINS OH COOUMAWAItt UNIt TOM HOTlBi* tOLOCATt* THAT COMFVAT* MMNAAt CAM At A. SfS0teCNSA-tt REFERENCE DRAWINGS >R0CtM F.tML AMOMTKWSttX.WttKOmT OUT *ROCttrr,yRACTOHATOWt*CTI8N,FfeCUr UmtVF g.<vc>, wyrtB.fiANtt >44 m. tftfUTV P.lLO, <T*AM4 COM&HtAU*UttTtS I 34A4 9 go* 4040 rtgtgVTt3xc-.mtrg yamLiw>*M^<^now Uir PtrtT.7>Trgw*.tA4*?3B iVytei p* utt or ttr in tm, |o-i4 A FORUM or MV. It* 0O.4*tJHt`i Are. [roCU*TCrtt>tP*ROlA^tA^-HPt ........ ... Twmnnrar KUlMgvntt. pH isstoA rot umm UCKIU CORPOKMION WHItAMOKO THS 7IXAS .COMPANY WIIHWI1HKI aL<* 6400__U *novt* IT mrulcol noM'ht*4bXfL PROCESS PIPING i INSTRUMENT DIAGRAM . COMPRESSION SECTION SA5 RECOVERY UUK 2525 4-RA-6IXI: ^?A-TEX 000778 A SSS (LfViSlON H9Ttt IAA AROYtf-THiA SUT ao l AeK1 SKjgj s! 3 7i t] 5* cCd iuniJ9 Hi A V I72^} A inhi REVISED PER DRAWING A'AA'iOL - REV.O rSc A w, 1350EQ FOR CONSTRUCTION r'c A ISfc UPOATCOTb^OO^LM*0 tSuo too Ao*eHMd_ MR 3* w ^3*1 ESSlwfeU- UAU | 0CRWI9 ORAN* BECHTEL GI2E3 TEXACO INC. FUGET SOUND PLANT PROCESS PIPING 4 INST DIAGRAM COMPRESSION SECTION GAS RECOVERY UNIT mam. wm nuanr. 3*m 4-RA-B 4/y 'VVWKIttf |8| 0M0 MOUHTCP (Lfc.LOCAL *OARB) dOWIAflt lit iitt lamumi* & wbsw.w.,, ---- ucciciai tuc !'-<1 OMiim tujiis < - i9fKrrr*nM >M4ffiuuiur no &nM.tvfmw9*t w J IM5y~gtf MCWT iPftffrflgATtgM Ail IWlfMf4fJ XBf *0919 fu UtetOIVCC *r|J* ttAhmo* mt * 9tt8 to* mK tr towuiw-tuj p.7T rood uamci iyn iivit tcamimitii* LIMi rpt witilC^>Otf~~ T m inns wnm vuomu* aw mwci oot uy Bt tfitCUUJIOi --------<?aV$t.w1------------ -- ----_.--_J* jsiinll ~~*j | niHrxwMKtitvw) 1 *--\Iit>ui tmftartttt*>,wotH yuwTvimBtrtcn) ^J'OKMOTCS TOMt) WWMB * ......... pP(*i#G9u<AMiHt {jurr-AoesDONC'imo pipimg ivtcihcAimf I'sT^tVftttJC^C*. I fa* C0104lM itWHMMCt" T*r ccttatiOK tuo*w*t MO*i CO<V,e.T.'t %>' COttOSlfif AUgglMt* w*Ki. i?U, c<T, X comCHO* uxowima *50**^.xr*3,C&. CtMlNT UHKtM M4MIV. X* Mft %HJ>VV*R . ^toibm5 AM Ot56WAttO $Y THE 5YM6014 SU0VM A**trfc, MlNpfl &VI*04S AM CltCttO NO JHCCUpt A T&tAHAUlAft. MAftC# ' 7. StftvteA *PCC>FfcATie?N* f&K. NEW UM65 A9t M AeedHPANCft WITH fiCW* J.-SOA TAftUt t. A tint tiUMAeil StfFFIte* fOi. moUUiTiOH aec ipfcuriftep a* foltow^t Pf> PEaAPmifii. fcPTcriotf CC Cc?t& CON5tttVAT10H fMt PAftTfAL UCAt COH5&*VAttp PHC FULL UtAT COU$ft.V4TlpM PTC OPBBAtIMtJi TftVPeHATl/BE COtiXeoO dT ATtAW TC4CBO AMP IM5UUt|0 All UP INSULAtlOK Twg* rbg^TfnaATra'R" Y'?'T^v"fA-Ml --IMSUtAllOM iJ p**Sj **** [ tfXACO OIIPIOIMUPIMWMACllAHIAISL suvict mcincAtioN ic ofo twin^y <gSKSKE*fct> -<EEH usmIaw*i iw * ECX'J iB-Ifc flCO) (sfAit nnnn) -nagar> -0532 "OSS It OM STOKASE (STAATUf>) cdfaMpoiiv fetAiijKiiigir wtgtpcu?xi.ug{/ip.yiw? .mt 41% IfMM I eOkO/KjAlT~ 4tvict vit fH | WW*T|B ~ tolilcV d^A^ig^T" IWCiUMlI-CWHWiiH WIT wottssi/g g>T.^rttwwww., ca fluoytrr w*t Ht MfcO* HUCSmJWO* *tcx.r K4U Vtn.tr P>- W*fU VxtTK-FCtV> vnviit >Mf- sitat coMmm-pu VTltllT Mffr ftffldlHHtll OH' fdv aalp. Wftfmtitytwfc uh-IKT.t uironttvinow van. THrt oftAynua (144 maty l.*V-l?*M MUUHiP >y ftMUtfinTiM KU^MlWi yWX*. 4. CWlTYUCht wtATHtAPXOOrfHO,. &TH9S (DMW VALVW . 04 COOLtwd v/Alt* AU1ALY H KtTtttM CltttS, Mi OlNA . tP.frU-lW % 10-PWfct. i i l} iI i ? ai tft riTvMai awoc Itt U-DMJJI 1600 C 2Es m. 4^ UvttlOUA tf *"----------nr- i f/\ S-R JOB No C-DIIO SHTNo 22213 DWS No 04-1-07' PROCESS PIPING & INST DIAGRAM ABSORPTION SECTION GAS'RECOVERY UNIT WlM ' | <w MPrtfl. ifOt >19 4-RA-7 IGA WA-TEX 000779 , -E-P-. CHECK .VAlVJt BB --t-fc-* FLU* VALVE TTTO*uay vuv* Bi) .' t ,, Hi wirrjtturr v*tve m -O j 5TTXT#JKAP m U*i Jfl? AFO APC r.o. Z23L [ Mft MRMt. OFE1M !1srfuA-ruutuea>xFiiint.ArDiaIMWoinU'XiLttMitCMiLt.taOi(tpVmwtt*/a ' SYMBOLS EXl6Tm& Htrt CiUOsfc . & SZfiLPCATfc %iOT UMP *qo mct aeuovt 0wft$ TiCMV UUft'fc&fc* motes I. REVISION* OP UAJD*. 6V6TCW5 AU Ol6NATE0 { JPYTUft &0WN AN?Y, UINOfc 2V6J0rt6 ARC CjRCt.t0 Ah IHCLUO& A t&AN&JlAR. RiVtfctON Mt*. t.pipmc* itavict specif*cations poa wfcv# uwe* , AKt IN ACCORPANCfc WITW G6MS 76&1.& 7. ' AUut UO. *UPFttfc* FORtHSUCATtON ON MftW UUfc* ABC iQfcNTlPlfcO A* PU.OvN<St { PP PERSONNEL PSdTUriON COLp OM*ftGvAT>OW PAaTtAb PEAT CONSERVATION prfu. WIAT CONSERVATISM 0POATlM6 `TEMPUATPaC COMfBOW PTCAM72ACtP 4 INSULATE V < c^iZ '3' c^Z ULi d O <0 I < cv I lO o* tO o cQ O "3 WA-TEX 000780 WA-TEX 000781 r 7.2 VESSEL DRAWINGS WA-TEX 000783 TABLE OF CONTENTS SECTION 7-2 VESSEL DRAWINGS Debutanizer - *B-C3 Tray Supports . Debutanizer - AB-C3 Trays . k-DC-25 4-DC-26 WA-TEX 000784 /so jg fi * it A A * I { A A i`i> Wv to* tCftlE sv. A/or **4- / A 7flL- /J Si/SO foe C-Of/Zm. % fcV** y 0*4. C. h rm. t*r. An*. 1 CEMOXED .A- drmdl/. HorrPAue BEOIITEL HOUSTON tixmoino: PUGET SOUND PLANT EXISTING DEBUTANIZER ITEM 4B-C3 ' TRAY SUPPORTS MNl Oa^H tfCKUL- 1009S TfXACftttt- 3010 4-DC-25 f*fc 1/ WA-TEX 000785 3A A jt 1 u 7.3 HEAT EXCHANGERS | \ WA-TEX 000787 TABLE OF CONTENTS SECTION 7.3 HEAT EXCHANGERS Summary Table 7-3"1 Heat Exchangers Data Sheets - All Exchangers WA-TEX 000788 ( TABLE 7.3-1 ' HEAT EXCHANGER SUMMARY TABLE GAS RECOVERY <JNtT PLANT 4B ANACORTES. WASHINGTON ' 3NSTRUCT10N DATA_________________________________ .__________________ No. -Shell Data iDiam. Material Passes Inches Material . No. Passes ______________ DESIGN_____________ Shel 1 Tube ~ Temp Press Temo Press V PSIG F PSiG 4 1 C.S. 5CR-1/2MO 4 4 25-1A 26-1A '^C.S. C.S, ' 1 580 450 300 75 500 150 650 300 650 75 720 ' 150 \U i ' * WA-TEX 000789 f ! EXCHANGER SPECIFICATION SHEET 1 CUSTOMER AND ___ PROJECT LOCATION "TP^LixfO lkl . plant pufiPT souwr>' 3 u EXCHANGER NO. 4B* ET1 CXCHANSER MPA. REQ. NO. ITEM NO 4 service OF UNIT LI&HT PTY fe0Llhl& TI7IM CQfHJSEL. 9 size 9J"* 7.40" 6 surface per unit TYPE CONNECTED IN Err. R. SHELLS PER UNIT f SERIES PARALLEL /) DO SURFACE PER SHELL <J^| EFF Gft PERFORMANCE OF ONE UNI T 7 1 FLUID CIRCULATED r 3 SHELL SIDE IT, TUBE SIDE dODUhiG lA/ATgfL os - j r(0*O P fP 8 ( TOTAL FLUID ENTERING l**A TL>OOP______________________ 9j 10 II j 2 !1 VAPOR LICUID STEAM NON-CONDENSIBLES / Oft. OA*7 TLAOO 13 ?i FLU VAPORIZED OR CONDENSED U15 \l } * STEAM CONDENSED GRAVITY-LIQUID 16 J VISCOSITY-LIQUID 17 J MOutCULAR WEIGHT-VAPORS w o.^sfrCm) / o.ut/"out) o, lIS (IU\ / .31 fPUT)______ ia ( SPECIFIC HEAT-LIQUIDS 19 \ . ATfNT HEAT-VAPORS 20 ; :t M**r rature in 21 j -C.MPERATUBE OUT 22 j OPERATING PRESSURE . PSIC /SO 100 . T.u/w mi/* *f TG fOt> 8 T U /* 'F *f .23 NUM PER OF PASSES / VElOClTY l PRESSURE DROP Au.ov/cALG 3 26 |yO..MIN6 RESISTANCE MIN. 0.001 27 26 $H`4T EXCHANGED-8TU/HR 1,7^0, ODD FT /sec 0 /*0 IN. 4 4.45 .5 * 903 N T.D. ICORRECTED) 7.1.G ft/sec -f/so in 29 RANSFER RATE - SERVICE CLEAN ACTUAL FQULtNO FACTOR 30 | OfStGN PRESSURE 31 TEST PRESSURE 32 DESIGN TEMPERATURE 33 TUBES 34 t SHELL CONSTRUCTION nsro */**m */0. IN. ___________ 580________________1_______ NO 0.0. two. SSt. LEnCTH I.D. 0.0. THICKNESS 't f? PITCH F/SQ1N w/so in rF 4 1) O') 35 SHELL COVER 36 t CHANNEL FLOATING HEAD COVER CHANNEL. COVER 37 ; TUBE SHEETS-STATIONARY 36 ' RAFFLES - CROSS 39 i BAFFLE - LONG 40 | TUBE SUPPORTS 41 | GASKETS TYPE TYPE ` FLOATINO THICKNESS THICKNESS THICKNESS 42 1 CONNECTIONS - SHELL - IN cur U" 43 1 -CHANNEL-IN lx 49 our /L'' 44 CJ CORROSION ALLOWANCE-SHELL SIDE MATINS RAT INS TUBE SIDE 300 iK-b*ti.F - 45 M CODE REQUIREMENTS TEMA CLASS SPEC 46 WEIGHTS - EACH SHELL OUNOi-C FULL OF HATER 47 NOTE INDICATE AFTER EACH RANT WHETHER STRESS RELIEVED .IS. R.l AND WHETHER RADIOGRAPHED (X-N) 48 . "rwARKS - TH)S /.<; Aki t--llyr/w & Z=*l77/v6 - TbU~ OJUA. WAL SilK-VlCC WA4 UgrE7WAMl:zSR. 7 nd CHlCULADKlfli Ttt=FLUi. fODLL-H-. FOR. DhTfe NOT -2>i4lLfeJ N /4I='P,t?n_ TD Dh7H SH&ST ^S^S D5-4--E-"? A DATA *a JL Ls^Ugt> FPR. OMSTlUiCTJDb* JOB NO. DRWG NO. REV. JP0^5 ds-4-e--4 O FORM H \tG PANT 8 9 /6 0 WA-TEX 000790 ( EXCHANGER SPECIFICATION SHEET 5 CUSTOMER .AND TG**ACO> IWC . II PROJECT LOCATION AKl fUDfLYla <. VO A EXCHANGER MFR. ] PLANT PURIST SOOkto PLAkTT REO. NO. EXCHANGER NO. U B-l? _______________________ ITEM NO - 4 SERVICE OF UNIT ABSDR-B15 fl-- bl gTHKHIT-gR.... STM. RgBOlLgff. 5 Size TYPE CONNECTED IN SERIES PARALLEL SURFACE PER UNIT ^ SHELLS PER UNIT * SURFACE PER SHELL /*> l"7 F -6Jfe PERFORMANCE OF ONE UNIT SHELL SIDE TUBE SIDE 7 1 FLUID CIRCULATED 0 TOTAL FLUID ENTERING 9 1] VAPOR iBS/Mt ASfrPnggR. R104 OU- ________ S~7t?AhF|_____ HO*.310_________________________ ________ LS. ________________________ 10 B LIQUID 11 U 12 jj STEAM MON-CONDENSIBLES 13 M FLUID VAPORIZED-Oft CONOENSED 14 STEAM CONDENSED 15 GRAV IT Y - LIQUID 16 ' VISCOSITY LIOUID 17 MOLfCULAR WEIGHT-VAPORS - 18 } SPEC'FlC HEAT-LiOUlDS 19 . -VENT HEAT-VAPORS 20 jj - fc M pr. R ATURE l H 2 I \ E. MPE RATURE OUT 22 J OPERATING PRESSURE PSIG 23 NUM BER OF PASSES VEt OCiTY ,| PRESSURE DROP ALLOw/cAtC 26 3 rOJt iNG RESISTANCE MIN 27 -U3.U7U O.Sl IT.u/4 ILD 8.TU/# ______________ 1LO 300 *f *r _____________ 133__________________________ FT /SEC P /SO IN 1L7,000 ru.ooo IV.O ITll/ e tu /+ UnO *f UoD *f _________ 12^_______________________ FT /SEC P/SO IN 28 8-i`ct exchanged-btu/hr 29 i TRANSFER RATE- SERVICE | '1*2..S'1^IOu m t.o. (corrected) CLEAN CONSTRUCTION ACTUAL FOUUNf* FACTOR 1 DESIGN PRESSURE P/SQ.IN */ SO IN 31 TEST PRESSURE 32 DESIGN TEMPERATURE p/SO. IN F P/SO IN *F 33 tubes 34 * SHELL no oD bwg Sit length 1.0. 0.0- THICKNESS pitch A <1 O <3 35 SHELL COVER Y CHANNEL FLOATING HEAD COVER ' CHANNEL COVEN J TUBE SHEETS - STATIONARY FLOATING 38 1 BAFFLES - CROSS f BAFFLE - LONG TYPE TYPE THICKNESS THICKNESS 40 TUR SUPPORTS 41 |GASKETS THICKNESS 42 I CONNECTIONS -SHELL- IN *2__ g1' 43 i -CHANNEL-IN C. '* 44 'J CORROSION ALLOWANCE -SHELL SIDE 45 J CODE REQUIREMENTS OUT OUT 1.0 " U" RATING RATING Tuae side TEMA CLASS R.P SDD IZP SPEC 46 WEIGHTS - EACH SHELL UMOLE FULL OF WATER 47 NOTE INDICATE AFTER EACH PART WHETHER STRCSS REtlEVEO IS N I AND WHETHER RAOIOGRAPHEO (X-R) 46 _r_M_ARKS - IS.SUED TO SMOulJ OPlUV7WW i PgR. TlZi^KlD i ITST, - TOR. DtaUA/M gPKJDl7iOKl< RVyCtiT^ TO DWrfl SHtitaT 2-feiSr ds- u~u?-<y - TOP gOV^VM . TVBgL-..Rfffrlfryiaa_____ 0* > _A- t)TC AUCl _A tI 1&. rnt. JSliVVSQ F9&.,,CFHSrRVf7H>N m. - JOB NO DRWG NO. REV. os-Ii-lr-3 0 FORM H.1SB PART B 9 /6 6 WA-TEX 000791 EXCHANGER SPECIFICATION SHEET | CUSTOMER AND | B PROJECT LOCATION Tstcax.^ Im<c ' J PLANT ~ POOET SoUMO / EXCHANGER NO. 4B- E.BO 4 5 SIZE 25 * 240 TYPE A.E.& EXCHANGER ' wfr. Hucmes* Ahoer^qh "REP. NO. E-<SZ ' "____________ ITEM NO Tf CONNECTED IN SERIES PARALLEL SURFACE PER UNIT 1 2. 1 S SHELLS PER UNIT | SURFACE PER SHEU. |218 ^ PERFORMANCE OF ONE UNIT SHELL SIDE TUBE SIOE 7 1 FLUID CIRCULATED 8 4 total fluio entering 9j VAPOR LBS/hr Splitter Fled 18,^39 a 27,59 8. Sputter Fee-ta ao. 351 . 10 1 LIQUID 11 I STEAM 12 tl NON-CONDENSIBLES 13 j FLUID VAPORIZED Oft CN06NS6D 14 j STEAM CONDENSED \ <2>0,a0 O 36^342 ao.35) 15 j GRAVITY-LIOUID c,p. Li 16 1 VISCOSITY -LIQUID ' Cp O.Cbcb.2,Oh> - o.C"7 (Out i 0.21 SHn}- 0.222Coot) A. PI E&.4 O.\fc,S HtO - O.ZS (Out* 17 -i molecular weight-vapors aCbtlNi - 8>3.8>tOof> 18 *| SFECIFIC HEAT- LIQUID5 19 J i.ATEtyT HEAT -VAPORS b.t.u/w . BTU/F .8. T. U /# 8TU/# 20 ij TEMPERATURE IN 2.1 \ TEMPERATURE OUT 22 ? OPERATING PRESSURE .23 NUMBER OF PASSES . - a VELOCITY PSIG 1 PRESSURE DROP AlLOw/CALC. 2<3> 2*7 <> 51 1 Co. 5 / G>. O -F *F ft. /sec. # /so in. 3-5 33 OC> M T. D. (CORRECTED) 52 8 29 TRANSFER RATE- SERVICE &3.Z CLEAN CONSTRUCTION ACTUAL FOULiNf- FACTOR ! DESIGN PRESSURE TEST PRESSURE | DESIGN TEMPERATURE tubes CARBON Stsel no H shell Carbon Steel. 2>1C=> |0 */SQIN. 225 t/so. in. 500 *f o.o.44*." efoa,0&S5?S: length i d. o?e. 25 %*a.* thickness 300 450 <3550 24-0" pitch J" #/ SO IN */S0 IN -f m *&<> i shell cover Carbon S.-re.ei- floating head cover Cmlbon Steel TUBE SHEETS-STATIONARY CARBON &TEEU FLOATING CARBON StEEU BAFFLES - CROSSCAMEt&.Ci.M lTgEL. U BAFFLE - LONG 0 TUBE SUPPORTS TYPE S6YASMTM-.<yTHC*NESS TYPE THICKNESS THICKNESS S gaskets MetAl Jacketed Asbestos ; M CONNECTIONS - SHELL - IN JO" OUT 12" tj -CHANNEL-IN 4tt OUT 4* W CORROSION ALLOWANCE-SHELL SIDE ~T7T p COOc REQUIREMENTS A&tAg. *3E1C.TIfstsl \/111 TEMA GLASS RATING ISO* RF RATING 3QO*RF TUBE SIDE F2 'Fg" SPEC. WEIGHTS - EACH SHELL BUNDLE FU.LL OF WATER MOTE INDICATE AFTER EACH PART WHETHER STRESS RELIEVED tS.R) AND WHETHER RAOIOGRAPHEP I X-R) remarks - fQ Baffle. Cot 44%. IQ- Ba.ppi_e<^ <S> 21 >pa.on. <1t> ~Th Exchaqaer. ~r Static Out-v Qviecl &x>4,tval E.x<mvtJag.g 3e>. E.7 51 mw U>i JL. A 0T A Revised , Icmjed Foa Coust Issued F=>k Riqchase VC JOB NO. DRWG NO. REV. -vi r~ -?K---------- XJi$. lOO^S DS-A-E-I 1 _ i_ * WA-TEX 000792 EXCHANGER SPECIFICATION SHEET I CUSTOMERAND R PROJECT LOCATION ~T~g.sc/x.Cga Ina. Bplant______ _______ J'""exchanger no!" PU6ET SOONQ 4B7- 51 SERVICE OF UNIT SPUTTER REBOILER SIZE. Z<Z> 240 TYPE AMT CONNECTED IN SURFACE PER UNIT 1222 EFF. SHELLS PER UNIT I EXCHANGER , - Aupg-tt^e>m__ I REQ. NO. E.-Q2 |( ITEM NO 2 SERIES PARALLEL SURFACE PER SHELL 1222 EFF /OR. PERFORMANCE OF ONE SHELL SIDE unit; TUBE SIDE 7 1 FLUID CIRCULATED . Gasoline Spuitter Btms. 8 4 TOTAL FLUID ENTERING 9j VAPOR LBS/m 2&2, 400 5C>,500 10 3 LIQUID 225 ,900 11 1 12 jj STEAM NON-CONDENSIBLES H fluid vaporized sr eEmsewsED j] STEAM CONDENSED Bfc.SOO PCC.O BTMS. QUE.NC.V4 122, 300 122,900 15 [j GRAVITY-LIQUID 16 fj VISCOSITY-LIQUID Cp O* <o <3? 0.0079 CVa.p> / O.lCaC UeO 17 MOLECULAR WEIGHT-VAPORS 129-fc f| SPECIFIC HEAT-LIQUIDS ' B.T.u/* y LATENT HEAT -VAPORS B. T U /* 20 j1EMPERATURE IN 21 | TEMPERATURE OUT 22 | OPERATING PRESSURE PSIG 3&>7 3 3 O- 40 Cn> - O.Cb&<OLrr> <0<oO 545 44& 1.0 t S..O 0.003 B T U /< a tu/f *F -f FT /SEC * /so IN 28 ^ heat exchanged-btu/hr E,0 00000 29 TRANSFER RATE- SERVICE 5i-2> CLEAN m t.d. (corrected) 20<b ACTUAL FOUL.NP FACTOR 30 3 DESIGN PRESSURE CONSTRUCTION "7S */SQ. IN. .. ISO */SQlN 31 TEST PRESSURE - 115 IF/SO. IN. 225 f/sq in 32 3 DESIGN TEMPERATURE CbBO 33 tubes 5%Cl- x,Z. % Mo no. 31TEEl. 1. D.-Of*. ZQ> 4 SHELL COVER S % OR. - ^2 % Mo ' *F 720 *f S! length 240h pitch I" THICKNESS FLOATING HEAD COVER 5%CR-,/2%Mo CHANNEL 5 % Co. - V-2 % Mo CHANNEL COVER G,STEei. V//5CR LlNERl 37 floating 38 I BAFFLES - CROSS Carsoki Steel type ^plio THICKNESS 39 baffle - long Carrod Steel typeMultileaf thickness 40 a TUBE SUPPORTS THICKNESS 41 3 GASKETS WCTAL X/yCICETEO ^BESTOS 42 H CONNECTIONS - SHELL - IN 2 - t*.' out 2 - 12 w RATING ISO* RF 43 -CHANNEL-IN OUT 4-" 44 W CORROSION ALLOWANCE -SHELL SIOE i/a* ----------------------------------------------------- ......................' ............. ii.7OTi.:Ni7i .rCm.iT5L. i.., 45 CODE REQUIREMENTS &SME. SECTION VtU PI TCMA CLASS RATING 300 3* RF TUBE SIDE */&'* ON C.<^~ R SPEC. 1 M~7 46 WEIGHTS 7- EACH SHELL BUNDLE FULL Of WATER 47 48 I 51 MOTE INDICATE REMARKS AFTER EACH PART WHETHER STRESS RELIEVED tS.R 1 AND WHETHER RADIO GRAPHED C X-fiJ geaoiLER Stacics OvgR 4E>-EI3>1 E.y.\yr\^o ^_____ "_____g- ' '' -miA A R.E.'JISEDj IssiSD Foe Co*>sT A *7Z lasusb Fog FbgdUAk^g. -&J- JOB NO DRWG NO I REV. J----10095 ps-4-S-2| 1 FORM H -IBB PART a 9 /6 6 WA-TEX 000793 7.4 PUMP DATA AND m-TEX 000794 TABLE OF CONTENTS SECTION 7.It PUMP DATA AND CURVES Summary Table Data Sheets - A11 Pumps Pump Curves A11 Pumps WA-TEX 000795 TABLE 7.4-1 CENTRIFUGAL PUMP SUMMARY SHEET GAS RECOVERY UNIT PLANT 4b ANACORTES, WASHINGTON < DRIVER DATA ia. Number of Shaf t ax. Stages Seal KPH H.P, Type Full Load Amps i 7 3600 , 7-1/2 Motor . Turbine 10 I |l-l/2 J3-7/8 * 1-1/2 Mech 3600 100 Mech Mech Motor Turbine Turbine Turbine Turbine WA-TEX 000796 ^ wrwiNbK.^ CENTRIFUGAL PUMP DATA SHEET OAPPLICABLE TO: PROPOSALS PURCHASE O AS BUILT O NOTE: (^INDICATES INFORMATION TO BE COMPETED BY PURCHASER; JOBN0.Afi&*i5--ITEM IUf4r&" <3fS. V G*SA PURCHASE ORDER NNOO.J.iLAQ..OOiill 5.....- &Q$_ ^ REOUISmONNa.............. ................... _... INOUIBYHO.___________ ______ .. J- . BY MANUFACTURER FOR . TgXACCx ImE" . DATEREVISION- . UNIT----------CtRMDE. C-VLP>JS.-M*Ar>WA__________________ SERVICE 2j S-5 .S&P ARA.TflC-- V-t QALP NO. PUMPS REOO_2=_NO. MOTORS REPTI.... \ ITEM MTI 4-&~G< g PROVIDED BY--iLAiVti LlAMTD BY.J5r_K,t3t>.T, NO. TURBINES REIYB \ ITEM NO PROVIDED BY E.mytuOfr. MTD BY _^XL.feT PUMP MFR UttlTe-O- RT- A.________________________ SITE ANO TYPE g" ftv SERIALNn ~l A A.Z5 ^ 2 OPEPIATING CONDITIONS, EACH PUMP i-L&ftT vvo LIQUID. -U.S,6PMtPT.N0R._ -RATED. -OtSCH. PRESS. PSI6_ 'hl'L .a FT. F. NOB.iAlfE.MAX.--------------- SUCT. PRESS. PStB MAX_J^--RATED. 2 8S.^ SP OR. it FT--<?5<Z>A---------- DIFF. PRESS. PSI- , VAP. PRESS. M FT, PSIA 2>OP niEF READ. FT $ %f--__________________ _________ '__________________ VIS. it PT. Rh_2l^j>.C5iBP______ NPSHA, FT~7 8 CORR/EROS. CAUSED BYHYD. HP .4 l"t. PERFORMANCE PROPOSAL CURVE NO. *51 L S7QAi ,y hpm-S.52J5l- npshr iwateri____ fjQ_.. FFf RHP RATED MAX BMP RATED IMP 7 * AMAX HEAD RATED IMP I ^ O MIR CONTINUOUS GPM_2lQ________________ ROTATION 1VIEWED FROM CPLG END). g-OP-^J CONSTRUCTION SHOP TESTS NOSIES SUCTION DISCHARGE ' SIZE 4-" a-* RATING "?> o o ?00 FACING Rf K.T LOCATION QNDN-YWT.PERF ENb ONON-WIT HYDRO ONPSH REDD TOP_______ jOSHOP INSPECTION OW1T. PERF. OWIT. HYORO OWIT. NPSH -SPLIT- AXIAL BRAD: TYPE VOLUTE E3SGL QDBL DIFFUSER PRESS: MAX.AllOW.-5L33_PSIG___ Q?L I: D HYDRO TEST 30^-- .PSIG jOOISMANT. AINSP. AFTER TEST OOTHER. _ . ... -CONNECT: OVENT DFRAIH DORSE ,, IMPELLER DIA: ORATED- MAX- DTTPE:Cm*l MOUNT: DBEIWEENURGS JZfOVIRHUNG D WEAR RS. OIAM./CIRNC------------- MATERIALS BEARINBSTVPE: DRADIAl_ifeilDTHRUStSMi-- APt CASE/TRIM CLASSQ- LUBE: BRING OIL jSjpLOOO OIL MIST OFUNGER DPRESSUHE COUPLING: DMBF_____ /TALlX. ________________ riMnnri 7~ V''/g7/?~ Tvspe\,t.afe... DRIVER HALF MTD BY: OPUMPMFR O DRIVER MFR OPURCHASER U-'VaCvft v)e Art. PACKING: DMFRGTYPE_______________ MECH. SEAL: pJtlPR A MOnPl /tJPAA/A ' pFB WPE & OSITE/NO. OF RINGS-. //?_____API CLASS. CODE RASEP1ATE: PI t) B. ^ VERTICAL PUMPS AUXILIARY PIPING PIT OR SUMP DEPTHO OC-W. PIPE P1AN- -OGU: OS.S.: OTUBING; OP1PE- MIRSUBMGIGENCEREQD.D__ _ --......... ....... TOTAL COOUNG WATER REOD. GPM_ . O SIGHT FJ. REDD- COLUMN PIPE: DFUNCB) DTHREADEO OPACBNG COOUNG INJECTION RED'D: O TOTAL 6PM QPS1G UNE SHAFT: DOPEN ENCLOSED OSEAl FLUSH PIPE PUN__________ OC.S. OS.S. OTURING OPtPE- BROS: DBOWl DUNE SHAFT OEXTERNAL SEAL FLUSH FLUID 6PM________________________________ OPSIG- BRS.IUBE DWATER DOIL DGREASE OAUXIUARY SEAL PLAN______ OAUX SEAL QUENCH FLUID- . OC.S. OS.S. OTUBING OPm- FLOAT A ROD OC.S. OS.S. OBRZ Ohone IftOAT SWITCH icXL^TLKMS, MOTOR DRIVER PUMP THRUST. LB DUP- . DDOWN- Jl'M PPM &6Q O FRAME ______________ VDLTS/PHASE/CYCLES -^hO/S/fecT GG..... .BEARINGS . &&AL------------ LUBE- GGe43f=.. type5V^.I5&^*. -INS_U__l.___ M2--FULL LOAD AMPS- ENC_ XP________TEMP RISE C_^2L -LOCKED ROTOR AMPS- 6o APPROX WT. PUMP A BASE____________ X OVHS OVSS VERT. THRUST CAP. It. . SERVICE FACTOR. MOTORTURBINE- mn iHcits# -- t v /-V UJv* Hr la ---------------- -- ? nfafcs 4T SU/AT- fSsi/2?>&!>AS$7~. / 7-7? issuers f=o rear, nod Jto 0 $4 2-73 1 S.SAJ6D 5=0 2- auOTKTIOfsi Vi. NO OATp RlUt. S POR- 140T SES JOB NO. DRAWING NO. REV. m inneiir DS-4-t-l 1 SHEET-- .J .OF WA-TEX 000797 CENTRIFUGAL PUMP DATA SHEET OAPPLICABIE TO: PROPOSALS PURCHASE O AS BUILT O < JNOTE. INDICATES INFORMATION TO BE COMPUTED BY PURCHASER- BY MANUFACTURE izAiyr/NG, fump'* JOB NotQDijSLlTEM Na.^B.6.9[r^.GSA. PUACHASEORDER N0.J&O.9 S/2 REOtNSITIONNO. .IQ.O. *}S G.r.OS' <*<=>/2 INQUIRY NO____________ ___ .. DATE_______ _____________ REVISION.-.................................. FOR . .... INC.______ UNIT. Recover uk>\t SITE--J StTCTCir ioi>ND .GLiseoturn. NO. PUMPS REO'DJ -NO. MOTORS RE0Y>_ LITEM NO.- PROVIDED BY_ NO. TURBINES RFirn ~-- _ITB NO- PROVIDED BY_ PUMP MTR UhJIT&h __________ (aLSIZE AND TYPE___ 6> -MTD BY -MID BY _ __ SERIAL NO..74.427/74-42S & OPERATINQ CONDITIONS. EACH PUMP U0U1D--Llhi'Ulp- -U.SGPMMPT.NOR_ //-.-C-,__________ -DISCH. PRESS. PSIG_____ PT. F. NOR-238 MAX- .SUCT. PRESS. PSIB MAX. SP OR It PT 0.57.1 -OIFF. PRESS. PSI________ VAP. PRESS. M PT. PSIA_.3i2.2_ . OIFF. HEAD, FT__________ vis. .1 Pi.Sw_^_3i2_ .CP_ -NPSHA.FT_____________! CORR/EROS. CAUSED BY... 3-2. L, -BATED-USi-SL LTL L4zSL >3' doppea&o -HYO. HP ..-33s-&\ CONSTRUCTION PERFORMANCE PROPOSAL CURVE No' TC-m TL~1 /TSTO NPSHR|WNTfnffl 11.1(2^5*t #2.5%*HPMTFH 47L*> ` SZ.MAX BHP RATED IMP________ G> ./SSL.MAX HEAD MTE0 IMP- MIN. CONTINUOUS RPM ~ ROTATION (VIEWED FROM CHS END)_ SHOP TESTS NOZZLES SIZE RATING FACING LOCATION OWIT. PERF. SUCTION DISCHARGE &" ROCr** er &.E. TOP .TO/9_______ OVY1T. HYDRO OWIT. NPSH ^CASE-MOUNT: (ft CENTERLINE OEOOT BUCKET VERT.(TYPE)- . -SPUT- Q AXIAL fc&AD; TYPE VOLUTE DSGL JSiBBl O DIFFUSER [QOISMANT. & INSP. AFTER TEST -PRESS: DMAX ALLOW.. 4rOC>...PSI6 _4l.f_ F: D HYDRO TFST-Cg-ClO --PSIS OWNER .. . -CONNECT: $VENT #FRAIN D6AGE IMPELLER OIA. nRATFtl I 3 '}uL tK MOUNT. BETWEEN BRGS BOVERHUNG PZALLBEARINGS-TYPE: TKaaohi MAX. WEAR. RG. OIAM./CLRNC. mvpf-Aasg/3 MATERIALS API CASE/TRIM ClASSO- iVBt tikmsciL anoaD Don mist dfunger dpbessure COUPLING: ffiMBE PA12-&/ 0MODEL `SJ5/J.C&J&' 7~*P'/cSjT. DRIVER HALE MTD BY: OPUMPMFR ODRIVERMFR O PURCHASER PACKING: DMERBTYPEDSIZE/NO. OF RINGS- pMECH. SEAL: MFB A M0Pa_^?/S' API CUSS. CODE--------- JKQmfr ocoe__ QP " />../__________________________ BASEPLATE: . VERTICAL PUMPS AUXILIARY PIPING OtW. PIPE PLAN- .Oat O.ss.: otubins: Opjpe- TOTAL COOUN6 WATER REQD. GPM_ . O SIGHT F.l. REITD- OPACKING COOLING INJECTION RIQ'O: DTOTAL GPM DPSIO OSEAl FLUSH PIPE PLAN__________ OC.SL OS.S. OtUllNS OPIPE- OEXTERNAISEAL FLUSH FLUID___________________ ____ D6PM________ OAUX1UARY SEAL PLAN______ .Ots. Oss. Otubing Op^E- QAUX SEALOUBiCH FLUID- MOTOR DRIVER | Ahp,,/.<ao .... .RPM. MFH... TYPE . ENC TPC, BAOVHS OVSS TEMP RISE. C. VERT. THRUST CAP. IE. . SERVICE FACTOR- PSIG- [PIT OR SUMP DEPTHO MIN. SUBMERGENCE RBrOD____ __________ __ COLUMN PIPE FLANGED OTHREADED LINE SHAFT: QOPFN ENCLOSED BRGS: DBOWL_______ LINE SHAFT____ BRS.LUBE QWATER DOIL QGREASF FLOAT & ROD OC.S. OS.S. ORBZ ON0NE FLOAT SWITCH PUMP THRUST. LB O UP- . DOOWN- APPROX WT. PUMP A BASE- MOTOR___ _ .TUR8INE iSk *5 /&5o>r> c&iTEL 7-L-12. iSSOBD. FOR CJtbiSTJlQCTtOtJ n>$v 13^ paft. puriua-svt i -*4-n tSSUE5b FDTL- QlfOrnrtPhf_ NO. DATE IN ML tea*, JOB NO. DRAWING NO. REV. pSvj-S-3 SHEET____ I------- -OF-----L WA-TEX 000798 t 1> CENTRIFUGAL PUMP DATA SHEET APPLICABLE TO: PROPOSALS O PURCHASE O ASBUIITO NOTE. (JINDICATES INFORMATION TO BE COMPLETED BY PURCHASER; a BY MANUFACTURER JOB koJUQ5T.ITEM H0 -4B- G 1^_ PURCHASE ORDER NO.______ ______________ * REQUISITION NO. .LOO/} - <* D 1 j5[l INQUIRY NO._______________ OATE______ ___________REVISION............................... mu -rdxAcb. I Mr. iiniTfiA& ReCOOgfty UhJIT /i^NO.PUMPSREOO-Jfe-lNO.MOTORSREOT)__ /___ ITEMNO.k&lA.tL- PROV1DEOBY PUHP.J^H&.MTD8Y P.UMP MF67& " NO. TURBINES REOD_J_ PUMP HER A- "HAM ITEM HO^B-GUA PROVIDED BY^XlSKlQ&MTOBY Pj/ilCHASU?R>- /Cl A.______ SITE ANO TYPE ---------- ------------------------ .SERIAL HO OPERATING CONDITIONS. EACH PUMP uauio. M &HT -U.aGPMatPT.NOR.. - DISCH. PRESS. PSIS_ _RATED_ 33 L PT. F, NOR--, t IQ MAX- .SUCT. PRESS. PSIS MAX.. -RATED____ I1*1* SP HR t PT 0.52. -EMFF. PRESS. PSI_______ I 8T VAP. PRESi at PT. PSIA_JLSlsZ___OlFf. HEAD. FT_ 7D___ <M VIS. at PT.SBtjeC-3Q._0P-_____ HPSHA. FT____ iD^c-oRlg^ CORR/EROS. CAUSED BY_______________________ _HYD. HP_a0.*O_ PERFORMANCE PROPOSAL CURVE N0. L .9J... RPM_3.5S!?-PSHR(WArEB|_A?-A r EFF...-5..&-3l.8HP RATE0__^2. MAX BHP RATED IMP 2 !.. MAX HEAD RATED IMP ^^4 MIN. CONTINUOUS SPM_ _UDl ROTATION IVIEWED FROM CPLG END) CCLVKi KCONSTRUCTION SHOP TESTS NOZZLES SIZE RATING FA0N6 LOCATION SUCTION 4 3 DO K.F TOP DISCHARGE 3 3DD CLP CASE-MOUNT: {&CENTERUNE OFOOT BRACKET D VERT. |TYPE)_ TOP SPLIT: D AXIAL ^RAD: TYPE VOLUTE DSGL $OBL Q DIFFUSER -PRESS: ClMAX AUOW fiTDC>. PSIG loD___ F: HYORQTEST_J_!L9.P--PStB L WSH REQ'O OWIT. PERF. y^ll. HYORO OWIT. NPSH lODISMANT.RINSP AFTER TEST bOTHER . .. CONNECT: DVENT DFBAIN DGAGE . IMPELLER DHL: PRATED____\SiJj4z____ DMAX____ IVx'L-------------TYPfcC.LO&gP MATERIALS MOUNT: O BETWEEN BROS 0OVERHUNG D WEAR R6. DIAMVCLRRC_________ S. BEARINGS-TYPE: nRUllAI RKLL. nthrust D(t- fttxl AH CASE/TRIM CLASSO- LUBE: l&fUNGOU DFLOOD POILMIST PFLINGER DPRESSURE S_COUPLING: riMRF F/\i>7 OMODa______________________ ftEM!,__ B^JU. DRIVER HALF MTD BY: OPUMPMFR O DRIVER MFR O PURCHASER PACKING: D MPR & TYPE . DSI2E/NaOFN^____ VECH. SEAL O MFR MODEL _Bi6i____ S-B- -Ml BASEPLATE FS - DtL- MFROCDE. VERTICAL PUMPS 2EAUXILIARY PIPING oOcw. PIPE PI AN v & ' O CU: S.S.; OTUBING; OPIPE_ D TOTAL C00UN6WATEB RED'D. GPM____________ . O SIGHT F.I. REQ'D. OPACKINS COOLING INJECTION RELYO: TOTAL GPM PPSI6 $SAl PLUSH PIPE PLAN 12. OCS. OS.& OTUBIN8 $PIPE S0CK?7 90.. OEXTFRNAL SEAL RUSH FLUID DSPM DPSIG- OAUXIUARY SEAL PLANOtS. OSS. OTUBING OP"^ OAUX SEAL QUENCH FLUID- MOTOR DRIVER HP-im. -VOLTS/PHASE/CYCLES 4 MFR-- A C ..BEANN6SL. J2ML. TYPE-I -FULL LDAD AMPS. JSL ' ENC-TAEA .TEMP RISE C SS tOCKFO ROTOR AMPS- OVHS OVSS VERT. THRUST CAP. IS- . SERVICE FACTOR- P1T0RSUMPDEPIHO 'MIN. SUBMERGENCE REQ'O.O----- ----------- --COLUMN PIPE: RANGED DTHREADEO LINE SHAFT: DOPEN D ENCLOSED !BRG& DSOWl___:__ DUNE SHAFT -- .. BRG. LUBE OWATEB DOL DGHEASE ROATBROD OC..S. OSO. OBRZ ON0NE nOAT SWITCH D PUMP THRUST. LB UP_______QDOWN_____ APPROX WT. PUMP B BASE, MOTOR- API STANOARD 610 GOVERNS UNIESS OTHERWISE Nilnra. Sts. ...APC.ttt?7 VgNLT 4 PYZthl Ki C QKlMlgOlPHii l i t * NO 130 IBEY1560 APRIL PI I fcjifiTVVT v.\ & T? g.A MW\>1- U 2.6 '% MQ3 NO. DATE PQIL P Xv* FQg. ttg-QV<>71~ Pm (?U a' h MTff- PKlveru to*. JOB NO. DRAWING NO. REV. zooms' ds-4-Gt-4 SHEET- .OF. WA-TEX 000799 2 t- v: t rvc* r\s m*' CENTRIFUGAL PUMP DATA SHEET APPLICABLE TO: PROPOSALS O PURCHASE O AS BUILT O m.lQ.0. iS.JOB ITEM N0-4-Br_&_3D.________ PURCHASE ORDER NO_______ _ REQUISITION NO. WA S.. ^ 7 ...... _ ' F./ * ~''1 \ NOTE: INDICATES INFORMATION TO BE COMPLETEO BY PURCHASER; 1NOUIIIY NO.___________ _________________ a BY MANUFACTURER DATE_______ _____________ REVISION...................... 3FOR hotrise UNIT. Af. Rgcoveay SITE. __ SERvicE_AiiSQ.SXlQB___QtL_C HAK.GU .PUMP NO. PUMPS REQ'O- -NO MOTORS REQTl. -ITEM NO- PROVIDEO BYMTOBY LNO. TURBINES REOTO___ -ITEM N0.4B=GX3OPR0IHDED BY_*^.M*:>fc.MTD BY T3. PIIMPMFR/K>GI?R.<OLt. - RA^m ________ SITE ANPTYPE..21 '/^ICfcJTA&r.^tj^ERIAlNP )g^S OPERATING CONDITIONS. EACH PUMP uquip-AB SP-P P-TU^N -U.S.6PMtPT.N0B._ -RATED- MIST __ QU_ DiSCH. PRESS, PSIG- j3Jiy_ PI. F. NORjLQIl--MAX------------ SUCT. PRESS. PSIG MAX. -RATED____ i SP ER PT___ CLJ3.5S_______ DIFP. PRESS. PS) 3-&L UJaS.VAP PRESS H PT.PSIA___I (a. l___ OIFP. HEAD. FT________________ Z3.vis it pt. sn.,,30iir__-i______ hpsha. ft______________ CORR/EROS. CAUSED BY___________________________________________ -HYO. HP. 05.5 CONSTRUCTION PERFORMANCE PROPOSAL CUBVENft-^Lm-fcS-IJ. RPM-J&SSO NPSHB (WATER)_L>.j'z/. \J\&,Eff 73/Q bhp RATFll MAX BMP RATED IMP____ L>J> MAX HEAD RATED IMP._l.SfeC>... MIN. CONTINUOUS GPM_ ROTATION (VIEWED FROM CPLG ONO) CT.V.I SHOP TESTS NOZZLES SIZE RATING FACING LOCATION OWIT. PERF. SUCTION DISCHARGE , SL '/a.'4 . RP 5iOE ONPSHREOD RE- - .i V E______ lOSHOP INSPECTION OWIT. HYDRO OWIT. NPSH CASE-MOUNT; OCENTERLINE WFOOT BRACKET OVERT.(TYPE) -SPLIT- ^ AXIAL ORAD; TYPE VOLUTE OSSL ODIl DIFFUSER PRESS. OMAXAIL0W..PSIGF; OHYDRO TEST__________ _____ PSIB ODtSMANT. & INSP. AFTER TEST 'OOTHER . .. -CONNECT: OVENT TRAIN DGAGE IMPELLER 01A.: ORATED MOUNT; ^BETWEEN BR6S OOVERHUNG MAX._____________________ WEARRS 01AM./CLRRC.- TYPE(%&. MATERIALS BFARINGS-TYPfc ORAWAI_____________________ _____________ OTHRUST___ LUBE: ORING OIL FLOOD OIL MIST OFUNGER OPRESSURE COUPLING: I~1MBF V>JAI-T7<2.0 MtlllEt 3A- , ~S^X ^ ^tgACCe. API CASE/TRIM ClASSO- DRIVER HALF MTOBY: OPUMPMFR O DRIVER MFR O PURCHASER PACKING: MFR* TYPE OSIZE/Ntt OF RINGS-------------------------------------------------------------------- MECH. SEAL: MFR* MODELAPI CUSS. CODE------------------------------------------ MFROCOE- BASEPUTE S> VERTICAL PUMPS AUXIUARY PIPING OtW. PIPE PLAN. -OCU: OS.S.: OTUBING: OPIPE- O TOTAL CODUNS WATER REO'O, GPM_ . OSIGHT F.I. REDD. OPACKING CODLING INJECTION REO'O: OTOTALGPM OPSIG OSEAl FLUSH PIPE PUN__________ OtS. OS.S OTUBING OP1PE- OEXTERNAL SUL FLUSH FLUID OGPM________________________________ Oauxiuaryseal pi am -OtS OSS OTUBING OP"E_ QAUX SEAL QUENCH FLUID. PSIG- pitorsumpdepthO MIN. SUBMERGENCE REQ'D. O------ -------------- ---COLUMN P1PL FLANGED OTHREADED LINE SHAFT; OOPEN O ENCLOSED BAGS: DBOWL_______DUNE SHAFT -. . IbRSIUBE OWATER ODIL GREASE FLOAT & ROD LlCS OS.S. OBRZ ON0NE FLOAT SWITCH . Dim Vvijr. V-z-SZrrJTA izc*><33 -TEMP RISE. C. APPROX WT. PUMP * BASE- VERT. THRUST CAP. LB. . SERVICE FACTOR- MOTOR_____ TURBINE______ APISTAMIARD BID GOVERNS UNLESS OTHERWISE HO^tTFOPA ft ^ JAC.?> *.. 7* TTmP PATTERFi 2gC-MTAC.tC/p vo.r^ AS/r 5wftC,'ip j R/ft tifeta;---------------------- ^tPL6cet> U>,-ru A UloPTy.ixM^T'ori qp?> H*A ^ i-r f mV? 0 l/Mr-.5 0 fckP* NO. DATE Fort. CmA.'i t>T(iOCT^-V I' Vk JOB NO. QRAWING NO. REV. toons DS-4-fe-S /SHEET-- -L. .OF. r> WA-TEX 000800 D CENTRIFUGAL PUMP DATA SHEET OAPPLICABLE TO: PROPOSALS PURCHASE O AS BUILT O NOTE. C) INDICATES INFORMATION TO BE COMPIETEO BY PURCHASER: BY MANUFACTURER J0BH0.IOOgi2.ITEM NO .ABr .6-3QA. PURCHASE ORDER NO._l.<SOl S. ~ Gu O \ REQUISITION NO.. JL.Q.O 3 5 INQUIRY NO.___________ .... . . DATEREVISION.. . . FOR UNIT. A.h& geco^ggy NO. PUMPS REO'D--l____NO. MOTORS REQ'OITEM NO.. Aftservice. SORPTION OIL CftKR&S PROVIBEDBYMTDBY NO. TURBINES REQ'D___ 1ITEM No48tfiI38A PROVIDED BY __MTD BY -Or*# > * PUMPMEN 0-1 -3T*-. SOT AMII TYPf-4- X.(aX\A SERIAI MB _. y 8 OPERATING CONDITIONS. EACH PUMP iinmo Lt 6>H T H , C --US. GPM M PT. NOR___U57. BATED --DISCH. PRESS. PSIB_____ 3 S>4-_____ ____ 500 PT.F.N0R_tOO_MAX.____ . SUCT. PRESS. PSIG MAX. SP SR M PT Ot~lb___ _3J-OIFF. PRESS. PSI_______ l VAP. PRESS. PT. PSIA_Jbjt2. OIFF. HEAD. FT_ JJJaSL VIS. PT. Su_3.0-L_CPNPSHA. FT____ IO.U _RATEDJ. CORR/EROS. CAUSED BV____________________________ -HYO. RE CONSTRUCTION PERFORMANCE proposal rnmif m &(> 4-T> -~A. BPMvlgSO npshr (WATER)_LC?_.... EFF._fiJfco_BHP RATED____&S.O____ MAX BHP RATED IMP ~3 ~S ~T___________ __ MAX HEAD RATED IMP l IQ O MIN CONTINUOUS GPM I "Z- O ROTATION (VIEWED FROM CPL6 ENDI C.P*J SHOP TESTS NOZZLES SIZE ' RATING FACING LOCATION SUCTION . (3 ?>oo*- 1? P To? DISCHARGE ___ ?>oo CASE-MOUNT: 3 CENTERLINE OF00T O BRACKET VERT.tTYPE) "To p SPUT- AXIAL DRAD; TYPE VOLUTE OSBt J^OBl DIFFUSER -press: hmaxaiiow goo psir.___A C2_ f. hydro tfst_L2=l&.o_psis -CONNECT- PVENT jifRAlH DGAGE OWIT. PERF. pUmT HYDRO Own. npsh ODISMANT. & 1NSP. AFTER TEST OOTHEB . . IMPELLER DM.. nAIfn U~Va MOUNT: j&BETWEENBRGS OVERHUNG RFARINBS-TYPE: nMniAt Bali MAX. 1$V&- WEAR RG. OlAMyCtRNC.. TYPE: C.^-Q'VeD MATERIALS THRUSTJUS____ API CASE/TRIM CLASSO- LUBE: RING Oil FLOOD OIL MIST FUNGER PRESSURE COUPLING; CTMRE ____________ MODEI--El. DRIVER HALF MTDBY: 0PUMP MFR jSfoRIVER MFR O PURCHASER PACKING: n MFB A TYPF ~ * ,. DSIZE/NO. OF RIHGS- nMECH. SEAL: MFB A MODEL p>VJ - API n ASS CODE__ Bs?T P ,,sS_ O MFR none fO > -2- -z. g 5P <VKL, P..-JLAL CASE - STgBl,. VERTICAL PUMPS AUXILIARY PIPING OCW-PIPEFUN^lBsseOCU: OSS.: OTUBING: OPIPEO TOTAL COOLING WATER REQ`0. GPM_____________________ SIGHT FXREffO! CA'AOtlHS COOLING INJECTION REQCfc TOTAL GPM DPSIS OSEAl FLUSH PIPE PUN...L3L. .. O CS. OS.X OTUNNS jfepiPE Sea $ O ^tec*. \Ug-P OEXTERNAt SEAL HUSH FLUID GPMDPSIS OAUXWABY SEAL PLANOC.S. OS S. OTUBING OP*"EOAUXSEALOUENCHHUIO UWgg. QGE.JC.A C.CHJ.J RteQ Q_ PITOBSUMPDEFTHO____________ ___________ MIN SUBMERGENCE REOUD---------------------- --COLUMN PIPE FLANGED DTHREADED UNE SHAFT- DOPEN ENCLOSED BRGS: GBBWL_______DUNE SHAFT _ BRG.IUBE DWATER OOIL GREASE FLOAT A ROD OC.S. OS.& CBRZ ONBNE (FLOAT SWITCH MOTOR DRIVER PUMP THRUST. LB DUP_ . DDDWN- HP___ . RPM_ -FRAME- --VBLTS/PHASE/CYCLES- MFB.. ___ LUBE_______________ TYPE. JRSUl- -FULL LOAD AMPS- ENC_ _TEMP RISE. C_ -LOCKED BOTOR AMPS- OVHS OVSS VERT. THRUST CAP-LR- SERVICE FACTOR- APPROX WT. PUMP A BASE. 5800 MOTOR F-W> g , _turbine^4D ' AH STANDABD BIO GOVERNS UNLESS OTHEBYhSEKOTEII Tvfj ~V0 QlVTFH^frTVY m a as et&>tr~ ;$$ij> /r&& e&JsK i `&S>4e.`D f&R. ftifejtc+A.-.S? o H-1-TL /St/PT frOEl OlAOTATIftA/ NO. DATE w }I JOB NO. DRAWING NO. REV. I009S DS-;48-<^ 1 SHEET__ /.--------OF------1------------ WA-TEX 000801 f -m CENTRIFUGAL PUMP DATA SHEET APPUCABIETO: PROPOSALS O PURCHASE O AS BUILT O NOTE: O INDICATES INFORMATION TO BE COMPLETED BY PURCHASER: BY MANUFACTURER monotOO9S'itfmwn *fS-&o/.A PURCHASEORDERNO.___ :_____ __________________ REOUISmONNO. \ .. . INQUIRY NO__________________ _____ . BATEREVISION... .. .............................. FOR UNIT. <5>3<r /gy /At rr SITE Ha PUMPS REffD_5L.N0. MOTORS Rum -- ITEM HO.. ROVlOEO BY- NO. TURBINES REOrO_J2_IIEM NO.- *f> -^oigjiinvinFn by ATx IS7/fiJ PUMP Mffi PllAGHAM a7P*Hntype* 5X4, -MTDBYutnav wn g235'5'^/223SS. OPERATING CONDITIONS. EACH PUMP PERFORMANCE LIQUIDS S.S. GPM *1PT. NOR. RATED___ 4-ZS PROPOSAL CURVE HOT?Aji&CGL PT F NOR JBO MAY SPGR.PT O.&Co VAP. PRESS, tt PT PSIA ? VIS. at PT. S 43^> CP SUCT. PflESa. PSIG MAX. RIFF. PRESS PSI OIFf HMD FT * l/P Arz. RATFfl' ^23 RFM-g.S^bg_-HPSHR (WATER|_LCL. .' MAX. BHP RATED IMP S"Q > *Z.______ MAX. HUD RATED IMP 4*1? g NPSHA.FT JO_______________________ MIN. CONTINUOUS EPM > Q CORR/ERDS. CAUSED BY.. _HYD. HP. ROTATION (VIEWED FROM CPLG END). CONSTRUCTION SHOP TESTS NOZZLES SUCTION DISCHARGE SIZE RATING 4- 300^ 3 FACING r RF LOCATION To f* OWIT. PERF. JSSjRT. HYDRO OWIT. NPSH CASE-MOUNT:^ CENTERLINE DFOOT BRACKET D VERT. (TYPE)-SPLIT: a AXIAL ^RAD; TYPE VOLUTE ^SL QOBl DIFFUSER -PRESS: OMAXALLOW._13- PSIG _L2I <?_ F: OHYDROTEST " Q Q___ PSIG OD1SMANT. 8INSP. AFTER TEST OOTHER .. -CONNECT: QVEHT &ERAIN DGAGE ., ______ _ . IMPELLER OIA.: PRATED I Q Tg <%] OMAX_ilL?-_ nnpg:,C-ffffpott. ED MOUNT. BETWEEN BROS ^OVERHUNG nwFAtt Bfi nuu yrJRHG A ?l *> T C> MATERIALS BEARINGS-TTPE RAHHI A L. L._____ nTHmiSrX?C-L-Ro-0 LUBE JzffilNG OIL OFLOOD DDILMIST DFUNGEB PPRESSURE COUPLING: l~lMRF P~ A `^'T" PMOBtt : API CASE/TRIM CUSSO P-ZM-7 P-Z.A / ........ DRIVER HALF MTD BY: OPUMPMFR O DRIVER MFR ^PURCHASER PACKING: D MFR 8 TYPE SIZE/NO. OF RINGS- MECH. SEAL: 1*1 MFR 8 MDDFL -O MFR DP-DP CU A- .API CUSS. CODE BSTF vS_ BASEPLATE . VERTICAL PUMPS AUXILIARY PIPING new pipppuH x)o^ pm- n; rvnmiHg- Vypipf TOTAL C00UN8 WATER REDD. 8PM O SIGHT FI REffD_ OPACKIN6C0DUN6 INJECTION REDD: DT0TAL 6PM DPSIG OSEAl FLUSH PIPE PUN 1 ~Z- O CS. OS& OTUBINS OPIPE OEXTERNALSEAl FLUSH FLUID. GPM_ PSIS. OAUXIUABY SEAL PLAN_______ OCS. OS.S. OTUBING OP'"E. OAUX. SEAL QUENCH FLUID. OOEAJCtA C-ox) k3EC.TkOaY r><vCPJ >*>.> ,.RPM_ MOTOR DRIVER .FRAME T.VOLTS/PHASE/CYCLES- UIBE_______________ TYPE- . ENC_ JNSUL -TEMP RISE. C_ -Rill LOAO AMPS- _lOCXEOITORAMPS_ 8 OVHS OVSS VERT. THRUST CAP. IB.- . SERVICE FACTOR- PIT OR SUMP DEPTHO MIN. SUBMERGENCE REffD. ____ ____________ COLUMN PIPE: FLANGED THREADED LINE SHAFT: QOPEN ENCLOSED BROS: DBOWl_______ 0 LINE SHAFT , BRG.LUBE QWATER DOIl GREASE FLOAT8 ROD OCS OS.S. OBR2 ON0NE FLOAT SWITCH ------------------------------------------- PUMP THRUST. IB UP- . DDOWN- APPROX WT. PUMP 8 BASE. 1?Q MOTOR_____________ -TURBINE- AN STANDARD BIO GOVERNS UNLESS OTHERWISE NOTBL. i! -------------- -- m H//4/7Z as RiuLf--rs>'sun Oa/s7T\ ? , 2 Atoeb iJ&JD. data- tss. Pe ctrfsr. Tit & JOB NO. DRAWING NO. REV. \ trfnfn. "EsSi >fe*E> Ft>-. Rl fLC.VYr& n with? sSv>E.t> P5/&. QuotaTi > NO. DATE %Ah JL id /OOPS ^5-4B-Gf\ 2 SHEET----- }---------OF--l------------ WA-TEX 000802 EQUIP. NQ.4B-G 5/A oiei WA-TEX 000803 f WA-TEX 000804 Byrok l WA--TEX 000805 ( WA-TEX 000806 { WA-TEX 000807 l WA-TEX 000808 * k' ' * . SiSI'Sj-.''''-; l 7.5 INSTRUMENT DATA | WA-TEX 000810- I TABLE OF CONTENTS SECTION 7.5 INSTRUMENT DATA Summary Sheet - Flow Element Summary Sheet - Relief Valves Control Valve Data Sheets Table 7-5"1 Table 7.5~2 WA-TEX 000811 Flow Element Mn 4FE-100 4FE-105 Service Hvy Gasoline to 4B-C11 Abs. Oil Chg- Pump ' Oriflee Size 2.596 1.600 TABLE 7.5-1 FLOW ELEMENT SUMMARY SHEET GAS RECOVERY UNIT PLANT 4B AHACORTES. WASHINGTON Line Size 4" Sch 40 3" Sch 40 Meter Coefficient 50 BPH 15 BPH WA-TEX 000812 Tag No- 4PSV-20S 4PSV-206 ' ________ Service 4B-GT30 4B-E7 TABLE 7.5-2 RELIEF VALVE SUMMARY SHEET GAS RECOVERY UNIT PLANT 4B ANACOR-TES. WASHINGTON Size , Set Press 2" x 3" 3A" x 1" 300 PSIG 75 PSIG WA-TEX 000813 >. WA-TEX 000814 ( FLUID IWL1T PttO OUTLETfSIO MIN. 1QF6R.JMAX. MIN, tow. MAX* "K INLET TEMP. F tOPtfLlMAX. I OPEB. SP. GB. | u*ty#por MOL.WT. Th P r X FLASH I OPEN. WI*C..P. 100 0.91 % Z? m. CHIT. PRESS. Pc VAPOR PNEIOv OPEN. PLOW MIN. FLOW SIZING PLOW MAX. PLOW PLOW UNITS OP SIZING AP SHUT OFF A P MIN. Cv SIZING APS FLOW I MIN. Cv \ Cv*VALVE SELECTED FACTORS m. 6PM j2_ Z3&. to Si'VO 'in JA. M. lL K*r-.kS- PRESS. RATtNO SONNET TYPE PACKING lubricator TYPE CONN1CTIONS 31 ^Od1 CLASS touts ^jjui TYPE | MAT'S. ISOL. VALVE vra ?"1 &u<3tnr 8P sra m iJdO 1L. o.ib (e30 urn JLiL 33S- MA khL MmsJA. xL fe~fcs?. lSLl. CTO ygs PONT SIZC NO. OP PORTS CHARACTER. PLUG TYPE GUIDE TYPE TNIM SPEC. ptcranr Ipwwto OPtfPClOSE HOW.OPBOCUmS ACTUATOR TVP1 kfel tffkHSbf rftP .AULMOTIVE POWER ILINEAR / ROTARY PRESS./VOLTAGC|POS* ON POWER PAIL] THRUST OS TORQUE RBL | SHUT OPpjoPSR JdLL A/Lj BtL'D gQO^gl ClJtg "OfA P. flip LihJ au. Ctofrg 1 cuy^ J2t^ JtdL 6/ ________ SIZE MAX. OUTPUT AX Manual q-rioe | pos. peeqsack type) 4Q_ o. POSITIONER OUTPUT I 8INGLE/0UAL =5-i/ INPUT SIONAL BY-PASS SUPPLY PSIO GAUGES M. ft- / P. O. NUMBER MANUFACTURER MODEL NO. | P. & I. O, NUMBER SERVICE XA. ti - 41> iifjgfL l*bl . `L-MrJL 3-sZ J-4ti fejis sThl&Ha .-pv |rai-&ic/u. c#ld j/vrrrp P.C-. gjilSfi ... fe*Ap>7&iiiiT_*__?__r Ye* -Yg J-4' Lui j..sr1 bwif A3-JzQ. 7 7.jgftrj5. LINE SIZE - NO. SPEC INSTRUMENT TAG NO. 4"- Jo>M3 4- i 2",.J.P fej.fi, 4-LV~ IQ v/ 1 VT-15 Ai>-j Cevr^/oaj rf A 0 14/.?^ HO. DATE &&&***& ... REVISIONS ORIGIN RAC ENG. CONTROL VALVES 4h4S-ie \Z_ . JOS NO. Ta OATA SHEET NUMBER REV. t " O- AO WA-TEX 000815 y- FLUID INLET PStO OUTLET PSIO MlN.lOPlBjMAX: MIN. iOPCR. MAX* INLET TfMI*. F toPER.IMAX. PEEK. SR. Git {uwvi*of MoJwT~ T*hFcr% FLASH I OPEN. VISC-^C.*. YiiTi u no iiL CHIT, PRESS. Pc VAPOR PRESS^w OPER. FLOW MIN* FLOW SIZING FLOW MAX. FLOW 0'<A ii. FLOW UNITS APSIZINO Afshut off & P MIN. Cv S SIZING APS FLOW | MIN. Cw C.-VALVE SELECTED FACTORS (m. toa US' iuii t3, 2. 9/ m Sft 1.2. M. Mt m i jll OA75 jlL. :Jrf\ M. Uk PRESS. PATINO MATERIAL SONNET TYPE LUBRICATOR TYPE CONNECTIONS CLASS BOLTS TYPE ISOL. VALVE l" 1 uoae Lr*>. $TC< . SdTTj. Sf>r iSPg /n*vi Vf-S y6 I :.s, ar NO. OF FORTS CHARACTER. PLUG TYPE OUIDE TYPE TRIMSPCa ACBW PUSHTO wwclcse ROW; oews^ious ACTUATOR TVFE JBL m iSStfTL ISfttfif "A...... f^SQ MOTIVE POWER (LINEAR / ROTARY ye 1 i^ [PRESS./VOLTAOEjpQS. ON POWER PAIL| THRUST OS TORQUE ERL j SHUT OPP OPER, SIZE MAX. OUTPUT JfL MANUAL O'niOE POS. PEEOSACK TYPE! 3a. 3o_ POSITIONER OUTPUT I SINOLS/OUAL 3~f INPUT SIGNAL BY-PASS SUPPLY PSIO GAUGES IzlL in K> .v'Aum Sli. Gjj.KA HdgoJ 11 I 3oo*:.. JZAl A*u _ira.. rcr-ft*i ,te?_ `Vc*. HL -W.fwi Sa vCpVo fefrift Qifip. AtA. Liu jjL ftuKgr m-tw ^ ft Pen M. R. / P. O. NUMSEft MANUFACTURER MODEL NO. P.S I.O. NUMBER SERVICE LINE SIZE-NO.-SPEC. INSTRUMENT TAG NO. Jfia. J-4-U Je.&.l, --U. Joial--3. MXJ1 SPEPT MBA 4^-*gmTA,^'A-fAfW i.J.-CLl___ 5LY-tt>( Z1* J3.f- 3'J3Z SLY-zaZ yLV- Z/0 J- 4-t i fl<-r -U_7 ro 4-CA-C, im >-'. t trj c-i._______ * JO^I'3 iSX: 7?.. 1 ( V'/'7i s0 s NO. DATE ORIGIN R&C ENG. 6e*J evistoio K^UcrO DCHK. Pj/^CriHe REVISIONS ftX.i-CC'* t."' ______3581.. X CONTROL VALVES f'CKJ: .-y ?-* c; *>jr -3lKks. JOB NO foods' OATA SHEET NUMBER DS - o - i-.i REV. WA-TEX 000816 7.6 TRAY LOADINGS ---------- ------------ --------------- ,m___ ________ - - -f~\ WA--TEX 000817 TABLE OF CONTENTS SECTION 7.6 TRAY LOADINGS Tray Loadings _________________Drawing No. V.P. 10095-C-52-HAC-1-2 V.P. 10095-C-52-HAC-2-2 V.P. 10095-C-52-HAC-3-2 V.P. 10095-C-52-HAC-4-2 V.P. I0095-C-52-HAC-5-2 V.P. I0095-C-52-HAC-6-2 V.P. 10095-C-52-HAC-7-2 V.P. 10095-C-52-HAC-8-2 V.P. 10095-C-52-HAC-9-0 V.P. 1O095-C-52-HAC-I0-0 V.P. I0095-C-52-HAC-11-0 V.P. I0095-C-57-HAC-J2-0 V.P. 10095-C-52-HAC-13-0 Table 7.6-1 ______________ Title Glitsch Perforated Tray F.W.G. 27711 - Sh. 1 of 8 Glitsch Perforated Tray F.W.G. 27711 - Sh. 2 of 8 Debutanizer 4B-C3 F.W.G. 27712 Sh. 3 of 5 Glitsch Perforated Tray F.W.G. 27712 Sh. 2 of 5 Glitsch Perforated Tray F.W.G. 27712 Sh. I of 5 Debutanizer 4B-C3 F.W.G. 27711 Sh. 3 of 8 Debutanizer 4B-C3 F.W.G. 27711 Sh. k of 8 Debutanizer 4B-C3 F.W.G. 27711 Sh. 5 of 8 Bolting 6 Clamping Assemblies F.W.G. 27711 Sh. 6 of 8 Packing List F.W.G. 27711 Sh. 7 of 8 Packing List F.W.G. 27711 Sh. 8 of 8 Bolting S Clamping Assemblies F.W.G. 27712 Sh. 4 of 5 Packing List F.W.G. 27712 Sh. 5 of 5 WA-TEX 000818 WA-TEX 000819 ' WA-TEX 000820 I t iS / ?'" - 81 ,A-}nP ^ Jr :W WA-TEX 000821 WA-TEX 000822 j WA-TEX 000823 I \Sl6`^IvcQ zz-tz-sm -yu. YJ~ WA-TEX 000824 WA-TEX 000825 ''C^yy j<s \:j~ WA-TEX 000826 WA-TEX 000827 WA-TEX 000828 WA-TEX 000829 WA-TEX 000830 WA-TEX 000831 Table 7-6-1 Tray Loadings Plant,- Gas Recovery Unit ' Anaco r tes, Washing ton Tray Nos. Tray Spacing, Ft. Vapor, CFS Liquid, GPH DEBUTANIZER 1|B-C3 Bottom Trays 1-6 7-21 2.5 2.0 23-8 22.1 1262 1209 Feed 22 2.0 15-9 992 Top 23-32 2.0 29-8 377 Oensity, LBS/C F Vapor Liquid Viscosity, Cp Surface Tension in Dynes/CM 1.89 3*t*6 0.13 6.0 1.81 3*).5 0.12 5.5 1.56 3**-9 0.12 5-0 1.51 32.0 0.12 6.0 WA-TEX 000832