Document M4k07e4zY7JdMJdBrMEKaROaL

m ADDENDUM TO OPERATING MANUAL GAS RECOVERY UNIT PLANT TEXACO INC. PUGET SOUND PLANT ESTIMATE 3910 BECHTEL INCORPORATED HOUSTON, TEXAS 1973 j WA-TEX 000754 V ) 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 .am WA-TEX 000757 ( I - GENERAL DESCRIPTION A. INTRODUCTION This addendum to the Operating Hanual 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 8. 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, 4-^RA-l and 4-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 Hanual 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. PistHlation 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 4B-GT30A 4B-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. 3,742 #/Hr. 8,510 #/Hr. 3,322 #/Hr. Cooling Water 4B-E7 ' Light FCC Gasoline Cooler 144 GPM Electrical 4B-G9 4B-G11 Absorber-Deethanizer Reboiler Circulation Pump Debutanizer Product Pump 47.2 BHP 51 BHP 3 WA-TEX 000760 I j 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 ,,^mh * 'TT?` .*P .twjf* 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 I 4. STARTUP J 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" 4B-0-376-2" 4B-0-350-8" 4B-0-351-8" Absorption oil bypass to 4B-C7 Rich sponge oil from 4B-C2 Splitter feed to 4B-E50 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-EI3. 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' 5 OPERATING FS. V ! WA-TEX 000768 i f 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 t r 6. SHufooW 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 `0 ( i 7. APPENDIX j ! WA-TEX 000772 I' 7. Appendix 7-1 Process and Utility Diagrams 7.2 Vessel Drawings 7.3 Heat Exchangers l.k Pump Data and Curves 7.5 Instrument Data 7.6 Tray Loading Data WA-TEX 000773 7.1 PROCESS AND 7 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 P&ID P&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 4-RA-l 4-RA-2 4-RA-6 A-RA-7 4-RA-8 . 4-RA-1l 4-RA-25 WA-TEX 000775 150 ikirn 77.500 C*M . too *510 2X0 ton UVHft tt*oo cm 31& V jia TWO 200 1=0'* *XO ** t 0le*1iM6 TW*OiHT w4Bt<Wlr iXt*lt . f'j$ erst 51000 <JPM JO*. .too fc>0 JUtt KMIHK HUH "SHT T*T" lit TltO t*r. AP&O iA.1V*. SOM> 07*1 * P 7>1 1*5*4. unw miihi -JUCH AMVWt. TO** AMIHt MJUSUrt *UW. Ut * jPXatHCXATIOM-VHIX. -%itK..j.w.^--a`te,TtE,Tww..a.J.B..t....,,....`.... --~yisgr^ oxatm&nur twnstit t Mt&tU lM4!at'tlSStHW>XtJt aotMMft 1 MftUTAMIftft -<SSK ftinigg>.Tg.wnwBtanwrsaw Mc-b ~332H> Bftcw.gitn nowm> S*S> -t5S2> Rg.Fg.S.NCE PtU,wm<a ftOQttW* frJUmUU<TtgW*tlX tHMW itqiW.Rttumy tstnv>wwUw,iMW.*nm.uy.,.ftift mtoinv unit ^iq,wTtwCTtflaTwiwttcnci.w.wiir >'% u !0 } WA-TEX 000776 3C?OR JOll>7lOU STORMCt UHt. - UO-rf sS2i mon iMjftcuoH 0mjho pump ' NUlfcS. * CA*k 'A 14 fOk OFItiTtOV tM W1CM 40 VOlUMt * 6+ 1H M 14 OUTIUAI* MktfCT c*\* V I# >0* OniAUON WMiCtf *W VOWMl * Of 1* tjtimn nrt> 14 OltTUlkfk MODUCf. pm At|'>r 10 At oncuttM <ou*io<*. *$. ovftM u>/t> a*k novneo ron of8qatkk4 wutatryr sPtiTrtQ xai ut fWe*U> tu iHii CAii.xtovv o TOTu FAX- CA404IM& I% CatlttO U PAaAtVt*rHctoj& iwt. vichi $ Mttwy aamiiue srftta}. ( REFERENCE DRAW fNG 5 PtOCtM Her* 0iA4UU^Uer>Mlt>M*F(t<lt UCt.TUlM) P*04{4 ILM procki fwn ntF <ta,eir-PovY vwr ttM A K* IKT ec <H47 JCT<M& 4MU P>0 Si Bf'5 & tot 11*1 OF C*t 4tllM **** 4 iM ii A-ftt >t CM4)tUC7>dUtttlW(i4 Pr r 'Mi K> im P# <!* MI 0X4 MU-I Mt A HUM# MR Uflovii. *44 mm*** " *" 5*l"'js *- HW* Httit Jww JlMWt it.QMi HCHTfl CORPORATION UNnVWKO THE TEXAS COMPANY MKMrtOVNPWOMS 6400--&____ PROCESS Flow DIAGRAM DISTILLATION i TRfcWWG SECTION GAS RECOVERY VWT Mlh. WMWIb 4-M-2-otteusca g&r 2525 `I WA-TEX 000777 la la nstfT" g TO A&5QRM.* OlfTHAMlttn CQUIMW *Q g to mamu pt-titawixot columw FCfcU O.H.vOOtP TO coot *>>_______ *0Oft Sittt '>0 *ttt 5UC64 OtUM -Sr5> a wtTHumtf-wi i n___r i OTCAfu mimwimi-g- punBwnn^ww1* mSTftUME.HT SYMBOLS UKUl. MO1MT0 SE TJUHMiTTlft *OAX MOUHT> munuM(m.cM cohtw>v *m UMC guccrflicM. u*o owvunv ruama = -PLANT HVHktA ~INTAVMCMT >t>MTJFJCATJC>N - mtTftUMtMT NUMMIl INSTRUMENT IDENTIFICATION ALL INTBWM*tr> *U C00*P WjAgCOgMMgC. WT t-i* ITAMDAKO* Utccrr A H07U> O* tltMK T 6Wfc M KCPlfc'4 ** UU*<Si (, LINE lOEMTlFtCATlOR ----{j5|555}-H2i JWHU& snCtfiCAIIOM -- tm* *zt HAMT MSbtCMTfL [ tlUtttfttAL Nt . HxiC6 WXKtMVUMmeM iuMT.antt(ttca) PIPING SPECIFICATIOH JD'Slk \ 170*11,7. yV C*W. MUW ~jbm nyo't.t cotm c.$. i/>orce<> J0LI t >00-r. dATt. Ct. AtlgwAMC* jofrn I >ooa..Cont.c.S.ft*,coit, auawak* ~jp.sti I not>,A7C,c.Vtt-***> ALL*Hgi jaw I so>fcr.goc^tg.s.yr>ca<. aubwamci jsftn 11 sa*y-p.&Ain.e.t. .Xfccatft-AilovAHt.i Jtw-itt } irg*mr.Umi7l>.fcATt1,C.t.CIM*W UwP4 joh1 5Qo*tc>c*jr^s, y* co*.AiLOvum$i. COMMODITY Pg-SJ&KATIOH Hvaicuinu,i>gwn v*m, >UA* stavto w7u COOCtM* WAtA *OU* W4TU ITEM NUMBERS N/ VI0T65 &Vi6t0* Qfi MAJOR. $Y*Tm> ACE: Qt4\6tNkTED OV 7t WUttOw* `MOftH Afeove. \iiK0St. RtV*J0N* Ltt& d:%cv&0 AMO Wui0& A TC>AM6UUA% RtVl^rOM fipinci 5C2vicc f^ecjpfcArow3 NEW UN3 ACC m ACC^COAh^C Y<iTH 6IM> *-T06 TASWC "7. . (.Mt klUUfrCK. ^liCFaCS FOA *Mu.CTi<9N ACC tUiKTifttO AC FOLU5*VC: OF Pft50NMt .PttOTfeiTlOM CC CiSUO COM^ftaVATI^ put PARTIAL hAT C^W&eftvAriON FHC FUU. JAT C<3HCVAT|^^ \ 0T6 <3PCCATtN6 TCmP^RATURC CSNTSOvj ST 6TCAM TjjAcgo AMO 'K'CUtAttP / Ml VO IMSU.ATIPN __ y LINE IDENTIFICATION I A -O-A, 2--04^-I-II5UAA-NI J t|Lot ` tu` t -iNSmATION IEQIMMMENTS (fTEXACO ttttNQ MAttkIAl NUMSE* 'SCCVICt 5SCC1SICATI0H ADDED \ , A8`ST-I3-3''.J34*PHC. ADDED ^ . VAUVE CODtf ^ 4-0730 f ~~------------- 1 /4-A J- DELETED 3Dt-N* t. APD&D YiC`>N *S*D,i01 >lL*t 3. A,peD P^-siGH NOTES t. i7ms t* *t >y*HiHo w vMd vm** ASSOetAtkd IC OS MAJftft taoi*MHT MAAKkP *. * % OkMHSOD AHb4k<CT T* %l lOC*TS AT i, vow ooi*r or vftCtsi. o> vxcl cTia* OftAtNS OH COOUN6 W ATU IIMAS IO (| OMfiU tOLOCATt* THAT COMOVAT* MAlNAAft CAM At A. SM0teCrt6>SA-t REFERENCE DRAWINGS ?XCBSP.tta AM0*m04SttX WtUC0<ttT PWT OCtSrr,U>FkACTOHATOWtlCWgW.FCCtfr UTHITT fetvt). WA'tgB.yVAWtS U tfttUT* y-fl.0. TTAM< C6M6HtAnmwfr*tVQ,>AVXtMAAtf S0A4ftia rtottirmiKVKin ratrosrxtMiwfr<g<naw >/7is<R>* uvr at itrrtt'gw>.4-gA^s> fj pof mt Ot Iff Alt OH. H41W G-L *>A{fOAU"1Cf AW. W QtQ.it>-Hl A Y//r>(nuoTortmtd*s6^A-fM p *!* P^'*l'MHWlm-n,aaMsmUMuLCJHT.AiaUr ' * "** whiwwiwun mcu sot AmovAi UCKm CORPOKATION MHItAMOKO THE 1ZJUS COMPANY VOOtMMWOtM PROCESS PIPING 4 INSTRUMENT DIAGRAM . COMPRESSION SECTION 6A5 BfeGOVEttY UUI1 2525 4-RA-6TO WA-TEX 000778 BECHTEL TEXACO INC. fUCrT SOUND SLANT PROCESS PIPING 4 INST DIAGRAM COMPRESSION SECTION GAS RECOVERY UNIT lumar* AH 4-RA-6 m ,>ak m aoAito MouurrtP tONUOt ill tut ------- -- f|N| HtfXIta jcKiumi* flPBSJSSJ.W uutfiiai leu umuflt tuttit ' HC>-StiStWllifl ....... iWMRUMgN-T^iottfttflgAffOM^...... AiVliutttOHtHl* AM W M ACMMWtf *11* M-4. tiApjuo? mm wpg. text imtt tttu ro4>*M# if.6. roaci u*uci wn uvn r<i<nuu~ ' ug tni uri^CAftolT~T~ tu uuu tfttm vtwttw* Mo otnmi wo* ut>n it cucvuttot . wr nW^R. Jtt( Ot$f6MATtO &Y TMR 5YM6CU* UOWVi AfrPvfc. MJWe?. tVl9f045 A 6l*Ct& 4&mcupc A TftfAtt&UUkft. OfcVVSiOM MARR* ` PlFlNCt seavteft *PC>PfCATIC?NS P4>*. Hitt UH&* M.I M ACCCfcPAXCfc Vfttrf *e* 4*$S tA&Ut t. 5v tint tJUMteft itf'Fitt* Ftf*. imutATloH au tpstirmtp *5 P#> PEAiOHnec CROtCtlOH CC cc?t0 CON5CVATlpM PMt PARTIAL UfAt COM5t*VATt0H PHC FUU. UtAT C7MS&AVAT)C>M 07C OPBffATlMrn TfiVpeitAruet <!CHT09O 5t AT|AM TAACBP AWt> IMAUUftO j M UA> >N5ytATI0N nrwtvieR.4--Ht K--Ut1f'MKtHKVffOic-JJtl { t-tuj utut w. {--ttHHwmwwif mur urrraffrca) ^ bsMOTCS wwikW ........... ' PPSH0,fi9U*>Alt $WAW>S& on C*JMK> pipiw^ 4PEci*t<:*tiotr >/ , C*.. 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CftftTYtC*U WtAiTHlXPKienMO, VTPM9 CttUM VACVt* MMc-txUMfLlilule4wnu *urM.Y- ***TUftU<utU8,ittmrtk tft twmt tcooC WUTIMA7I tCjQQC Stearns-Roger wtQrvHAJrt C7 3St f.<0Q_-fe.____ AtHO<l VI na&w' PPOitSS PtPtW6 l tHilAUMtUT DIAfiBAM ABSOafTJOW oas ftecovtzr unit 2525 ,4-rRkr: UXACO] fEXftCO ,nb. nmu _ * fuctr *CKiNia fLANT PROCESS PIPING l INST DIAGRAM ABSORPTION SECTION GAS'RECOVERY UNIT --rtu-t-t--m---*- y|*.t... 4-RA-7 IGA S-R JOB No C-IIIIO SHT No 22213 0W6 No 04-1-07 WA-TEX 000779 1 V Cd I u_i d O O I c<v i 'i ln CJ tO 0s1 cQ o "3 WA-TEX 000780 WA-TEX 000781 LEGEND i ~j \ I. NORMAL OPERATION ------- 1 4. POWER FAILURE < > &T6AM USAGE WHEN OPERATING > ( ~ *F ) TEMPERATURE 'F ALL FIGURES IN IOOoVhR. EXCEPT AS NOTED. j > 2 16.24 ZZ> l i > > 2 WA-TEX 000782 A A 'H' ISSUED FOR DESIGN HK o*w BUlillH * ** 4* tA * QM 04>***v. t*r. tJiH*S. Al*c. Si BESHTEL HOUSTON IMAGO INC. PUGET .SOUND flANT UTILITY USAGE DIAGRAM GRU UNIT ' PLANT 48 toooc i ItXACQBf- 3310 I 4-RA-25 |0A 7.2 VESSEL DRAWINGS WA-TEX 000783 TABLE OF CONTENTS SECTION 7-2 VESSEL DRAWINGS Debutanizer - *B-C3 Tray Supports . Debutanizer - AB-C3 Trays . 4-DC-25 4-DC-26 WA-TEX 000784 /so jg fi it A A AA A tCftlE * sv. A/or **4- / A 7flL- /j si/so foe C-or/zm. % fcV** y 0*4. C. t**r*.. An*. 1 CEMOXED .A- drmdl/. HorrPAue BEOIITEL HOUSTON I { tixmoino: PUGET SOUND PLANT EXISTING DEBUTANIZER ITEM 4B-C3 ' TRAY SUPPORTS MNl tfCKUL- 1009S TfXACftttt- 3010 4-DC-25 !* 1/ WA-TEX 000785 3A A 1 4j 1 it 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 UNIT PLANT 4B ANACORTES. WASHINGTON ' 3NSTRUCT10N DATA_________________________________ .________________ Shell Data No. iDiam. Material Passes '' laches Material . . No. Passes ______________ DESIGN_____________ Shell Tube ' Temp V Press Temo PSIG F Press PSIG . 4- 1 C.S. 5CR-1/2MO 4 4 25-1A 26-1A i'c.s. C.S, ' 1 580 4:50 300 75 500 150 650 300 650 - 75 720 ' 150 \U -! ' * WA-TEX 000789 f S FORM H \tG PART 8 9 /6 0 p fp o -J EXCHANGER SPECIFICATION SHEET 1 CUSTOMER AND ____ PROJECT LOCATION "TP^Lixf O IkH! . CXCKANSER MPR. plant puftPT souwr>' 3 u EXCHANGER NO. 4B* ET1 REO. NO. ITEM NO 4 service OF UNIT LI&HT PTY A0LlhiC TI7IM CQfiLJSEL. 9 size 9J"* 7.40" TYPE CONNECTED IN SERIES PARALLEL 6 surface per unit Err. *. SHELLS PER UNIT j IOOO SURFACE PER SHELL <J^| EFF Gft . PERFORMANCE OF ONE UNI T SHELL SIDE TUBE SIDE 7 1 FLUID CIRCULATED LIGHT FCC &APUM<= CODUhiC, WATgfL 8 ( TOTAL FLUID ENTERING l**A 7L>OOP______________________ 9j 10 II j 2 !1 VAPOR LIQUID STEAM NON-CONDENSIBLES / Oft. 04*7 7L.0 00 13 ?i FLU VAPORIZED Oft CONDENSED } STEAM CONDENSED U15 \l * GRAVITY-LIQUID o.Gsfrfm) / o.ut/"out) 16 J VISCOSITY-LIQUID 17 J MOutCULAR WEIGHT-VAPORS o, lIS (iu\ / .31 fpur)______ w ia ( SPECIFIC HEAT-LIQUIDS 19 \ . ATfNT HEAT-VAPORS .T.u/w v S.T u/w BTU /P ITU/# 20 ; :t M**r rature in 21 j -C.MPERATURE OUT 22 j OPERATING PRESSURE . PSI / 20 100____________ *F *r fOO -f *f .23 NUM PER OF PASSES VElOClTY l PRESSURE DROP 26 |yO..MIN6 RESISTANCE 27 Au.ov/cALC MIN. / 5______________ 0.001 FT /SEC 0 /SO IR. 4 4.45 S * 903 ft/sec 0/SQ IN 26 Jh`at exchanged-btu/hr 29 RANSFER RATE - SFRVICE l,~}^0. ODD S3 CLEAN N T.D. (CORRECTED) 2.1.U> ACTUAL FOULiNG FACTOR CONSTRUCT 1 O N 30 | DESIGN PRESSURE 31 TEST PRESSURE U5-Q ______ */som *7/T */wa.m. w/saiN w/so IN 32 DESIGN TEMPERATURE 33 TUBES 34 t SHELL NO .<580 o.o. two. I. 0. 0.0. . r ____ -E*sth THICKNESS 'ioD PITCH ~f A < OO 35 SHELL COVER 36 t CHANNEL FLOATING HEAD COYCft CHANNEL COVEN 37 ; TUBE SHEETS-STATIONARY floatino 36 ' RAFFLES - CROSS TYPt THICKNESS 39 i BAFFLE - LONG 40 | TUBE SUPPORTS TYPE THICKNESS THICKNESS 41 | GASKETS 42 1 CONNECTIONS - SHELL - IN 43 1 -CHANNEL-IN lx 49 44 CJ CORROSION ALLOWANCE-SHELL SIDE OUT out C /a * > RATINS RATINS TUOE SIDE /^ro^fc.F - 45 M CODE REQUIREMENTS TCMA CLASS SPEC 46 WEIGHTS - EACH SHELL OftOtC FULL OF NATEft 47 NOTE INDICATE AFTER EACH RANT WHETHER STRESS RELIEVED !*. R. 1 AND WHETHER RA0IO6RARHED (X-R) 48 remarks -7-HIS, /S AkJ t*UkTiHn. e*77/V& - TbU~ 0!U A NtoL SER-V/f C WA 7l/fc-irTMANlTtgR- up CHlCULADKlfli Rt=PLUi. fODLL-H-. POR. DATA NOT ia^Fi?a. td oath sneer isis --P.SrA:---&=3. a DATA z m a Ls^Uqt> PPR. C0KU-7ULI177PM JOB NO. DRWG NO. REV. IP0^5 ds-4-e--4 O WA-TEX 000790 ( exchanger specification sheet B CUSTOMER .AND TliHACOi IK/C . EXCHANGER N projectlocation AJvLAjCOi^laJ^ VQK SH.-------------------------------J?TM-........................... - - 1 PLANT py fa 1ST SQUKItS PLAKTT__________ 2 EXCHANGER NO. /l R -1? - PltiTlKI fii .......... ~ RE *> TtZiTnO 4 1 stRvce OP UN.T ABSDlLKElL-t>\ irrWKHILetL STM. RCBDtLffR. 5 Size TYPE CONNECTED IN - SERIES SURFACE PER UNIT /<TJ"7 SHELLS PER UNIT SURFACE PER SHELL / $ - ^! PARALLEL ^ PERFORMANCE OF ONE UNIT 7 1 FLUID CIRCULATED a 4 total FLUID ENTERING 9 i] VAPOR LBsAp Q LIQUID u STEAM n non-condensibles j FLUID VAPORIZED "OR CONDENSED J steam CONDENSED | GRAVlTY-LIOUID j VISCOSITY LIOUIO J MOLECULAR WEIGHT-VAPORS }| Sf-EC'FIC HEAT - LIQUIDS > 3 ..VENT HEAT-VAPORS SHELL SIDE ASSOUGisR. RICH OV- U 0%3lO Ab'.VUS aw.unw .. O.sl ItO t.u/* B.TU/P TUBE SIDE STlSAN^ LI*,00.0 1U.OOO ......... {fr.o 8T/F BTu/p ji - fc M pr. R ATUR1 IN < 'EMPERATURE OUT | OPERATING PRESSURE PSI HUM 1 R OF PASSES VEl OCiTY . | PRESSURE DROP allow/CALC rOJt *NG RESISTANCE MIN tU> 3O0 *f *F _________LSL2*__________________ FT /sec /SO IN MnO UoD ,L3>5' *f *f FT /sec p/so IN transfer rate- service 2?SIGN PRESS1J_RE_ r$T PRESSURE clean CONSTRUCTION */so,m #/ao. in ACTUAL FOUUNC* FACTOR 0D BWG . 0. 0.0. type LENGTH THICKNESS FLOATING HEAD COVER CHANNEL COVER FLOATING THICKNESS THICKNESS THICKNESS */ so in p/so IN *f A < OQ *1- S" 0T OUT /QM BATING 3&D'a tlF fe *:_______*TIM6 3P|> -a IZF TUBE SlOE TEMA CLASS SPEC BUNDLE FULL OF WATER EACH PART WHETHER STRESS RELIEVED IS A) AND WHETHER RAOIOGRAPHEO (X-R) * -Rr-M-Agl--.-. JbVD TO fiMOWH OPi2tU*7IH& CoHQ17/t>M4 PgRL TteUKLO .l>J&U2. - FOR. DgU4(st CPhtPiTiOKi*.. av/EMi-TD awrn smitrT 2JSJLS:__&5~ st - TOP 3 gQWA &E...TVBg.L EgM&Vtrto Wfi A t>Jf bt A t f [ittuttta Pott, <lpntorn.vcyit>i im - JOB NO DRUG NO. REV. toots os-u-e-z 0 FORM H-15B PART B 9 /6 6 WA-TEX 000791 EXCHANGER SPECIFICATION SHEET | CUSTOMER and B PROJECT LOCATION J PLANT ./ EXCHAN6ER NO. Te.'XAs.c.c^ POO&T GoUNO 4.B - E.SO EXCHANGER mfr. Wuciwes- Amoeg^oM REO. NO. -<S2~ "___________ ITEM NO I t~ ~ 5 SIZE ZB * 240 Z6. SURFACE PER UNIT 1 1 S TYPE A.E.> CONNECTED IN SHELLS PER UNIT | SERIES SURFACE PER SHEUL parallel |2l& EPF PERFORMANCE OF ONE UNIT SHELL SIDE TUBE SIDE 7 1 FLUID CIRCULATED 8 TOTAL fluio ENTERING 9 VAPOR LBS/HR Sputter Feed 18,^39 a 2f.59& Splitter Fc.e.i SO. 351 . 10 LIQUID II STEAM 12 NON-CONDENSIBLES 13 FLUID VAPORIZED OR CN06NS6D 14 STEAM CONDENSED 15 GRAVITY-LIQUID C,P. l_l 16 VISCOSITY -LIQUID ' Cp 17 MOufCULAR WEIGHT-VAPORS 18 SFECIFIC HEAT-LIQUIDS 19 * i.ATEtyT HEAT -VAPORS 20 J TEMPERATURE IN 2.1 1 'EMPERATURE OUT 22 j OPERATING PRESSURE PSIG 23 NUMBER OF PASSES f* ^ velocity l PRESSURE DROP ALLOw/cALC. 26 J FOULING RESISTANCE MIN. 27 l <2>0 , ao O 36.342 o.<o&2 0m>- O.OH (Out) 0.21 SHm>- 0.222Coot) &<bdlM3 - 3>&.&<LOo-r> B.T.U/W ,B. T. U /# 2Q\ 21Q> f #F 51 1 G>.5 / <S.o FT. /SEC. # /so IN. O.ool AO. 351 API 33.4. O.Ub5nN)- o,2S {Out* . . 39 8TU/# *F F FT /SEC * /so IN. 28 g HEAT EXCHANGED-BT.U./HR 5 4-SO > OOO M T.D. (CORRECTED) 53 29 TRANSFER. RATE- SERVICE S3.2' CLEAN CONSTRUCTION ACTUAL FOULiNO FACTOR 30 S DESIGN PRESSURE 31 TEST PRESSURE 150 - 225 */SQ IN. */S0. IN. 3oo 450 #/S0 IN */%a m 32 DESIGN TEMPERATURE 500 *F <550 ^4*33 tubes Carbon Steel no. 3lfe. o. o. efoa.oa55; length Z4-0*1 PITCH I1* *F A *ZtO 34 shell Car bom Steel. i. d. wo. 25 *74* THICKNESS 35 : SHELL COVER Carbom .-re.ev_ FLOATING HEAD COVER CP.GLBOM S.TEEL 36 channel Cmj&qfj Steel CHANNEL COVER CARBOH ^TESL 37 tube sheets-stationary Carbon Steel FLOATING CARBON 5TC.fi.t_ 38 baffles - cross Car bom Steel type Se6WlSNTAL.<rrHig*NEss________ 39 BAFFLE - LONG TYPE THICKNESS 40 TUBE SUPPORTS THICKNESS 41 1 gaskets MetAl Tacketed Asbestos 42 CONNECTIONS-SHELL- IN lO" OUT 12" RATING ISO* RF 43 -CHANNEL-IN 4-n OUT 44 i CORROSION ALLOWANCE-SHELL SIDE /S." 45 CODE REQUIREMENTS KGtAG. 5E1C.TI AN \JW 1 4-* RATING 300* RF TUBE SIOF. TEMA CLASS R. SPEC. 46 WEIGHTS - EACH SHELL BUNDLE . full of water ; 47 NOTE INDICATE AFTER EACH PART WHETHER STRESS RELIEVED (S.R) AND WHETHER RADIOGRAPHED 1 X-R) (\}48 remarks - Baffle Cot 44%. lO- Bafflee <S> 21 ^Ifi.* 6PACIN6. Tm Exe.HKtAC.ew, T*. <>t/us*. Qowy poese 2>g>- 5.7 51 m Ua>i 0*T A T4'll feevi.ED 3 Usocc. Foa Coovr. VS-*^ l-SSUEo'Fed FbacHA..e VC JOB NO. DRWG NO. Tit 7k---------- . Xrj$. lOO^S ds-/V-E~\ REV. t FORM H-198 PART 8 9 /6 8 WA-TEX 000792 EXCHANGER SPECIFICATION SHEET I CUSTOMER - AND I PROJECT LOCATION ~T~g.YtiN.Cga Ina. Iplant________ _________ J'""exchanger no!" PuoeT Sound 4B7- 51 service op unit Splitter Reisoit.R size. Z<Z> x 240 SURFACE PER UNIT 1222 TYPE AMT CONNECTED IN EFF. SHELLS PER UNIT I EXCHANGER . Viy ahe<. - Asoe.n^QH__ REQ- NO. E.-Q2 ________________ ( ITEM NO 2 SERIES SURFACE PER SHELL PARALLEL 1222 EFF /OR. PERFORMANCE OF ONE UNIT; SHELL SIDE TUBE SIDE 7 1 FLUID CIRCULATED . Gasoline 5puiTTeB.BTMs PCC.O BTM5. QUE.NC.V4 8 4 TOTAL FLUID ENTERING 9j VAPOR 10 3 LIQUID LBS/m 2&2, 400 5&,500 225 ,900 122, 300 122,900 11 1 12 jj STEAM NON-CONDENSIBLES H FLUID VAPORIZED SR etJN&EMSED j] STEAM CONDENSED Bfc.SOO 15 [j GRAVITY-LIQUID fj VISCOSITY-LIQUID 16 Cp O* <o <3? 0-0079 (Va.F>> / O.lCaC Ucv> API 1S. O- 40 Cn> - O.Cb&<OLrr> 17 MOLECULAR WEIGHT-VAPORS f| SPECIFIC HEAT-LIQUIDS 129-fc ' B.T.U/* BTU/f y iATENT HEA7 -VAPORS B.T#/* a Tu/- 20 .TEMPERATURE IN 21 | TEMPERATURE OUT 22 | OPERATING PRESSURE PSIG 3&"7 3 3i_T Flow 4- VELOCITY . FT /sec. 4.& FT /SEC J PRESSURE DROP ] FOULING RESISTANCE 26 AU-Ow/cALC. MIN. 1.0 / 0.50 0.004- ip/soin. "7.0 t 8. O 0.005 ^/so in 27 28 ^ heat exchanged-btu/hr E,0 00000 m t.d. (corrected) 20<Z 29 TRANSFER RATE- SERVICE 31-2> CLEAN ACTUAL FOULiNG FACTOR CONSTRUCTION . . 30 3 DESIGN PRESSURE "7S x/sq.in. ISO -f/sq in 31 TEST PRESSURE 32 3 DESIGN TEMPERATURE - 115 Q>SO */6Q.m. *f 225 720 jf/sq in *f 33 tubes 5%Cl- l/Z % Mo no. 31 4 SHELL COVER S % C-R. - *^2 Vo Mo ' S! length 2 40* pitch I" THICKNESS FLOATING HEAD COVER 5%CR-,/2%Mo 5CHANNEL % Co. - V-a % Mo CHANNEL COVER C.^TESt. V//5CR LlNERi 37 38 I BAFFLES - CROSS C.AESOKI STEEL. TYPE ^QLin THICKNESS 39 BAFFLE - LONG CARSOM StEEl TYPEMulTILEAF THICKNESS 40 tl TUBE SUPPORTS 41 3 GASKETS METAL X/VCICEIXEO ^BESTOS THICKNESS 42 CONNECTIONS-SHELL-IN 2- I 12. '* our 2 - 12 w RATING ISO* RF 43 _____________________-_C__H_A__N__N__E_L__-_IN_____________________ OUT 4- RATING 3QO ^ RF 44 W CORROSION ALLOWANCE-SHELL S10E /g*O___N_____C_ _.__5__. TUBE side /&.'* OH C.<^. 45 CODE REQUIREMENTS &SME. SECTION VtU PI TEMA CLASS R SPEC. El H~7 46 WEIGHTS - EACH SHELL BUNDLE FULL OF WATER 47 MOTE INDICATE AFTER EACH PART WHETHER STRESS RELIEVED IS 8 I AND WHETHER RADIOGRAPHED (X-HJ 48 REMARKS - TUI'S geaoiLER Stacks OvgR 4E>-EI3>1 E.y.\<yr\Ao ^___ _g- '' ' 51 A A RSn/ISEP , A-- `tm -71 iI_ss* us.b FF*og For CoMb"f 522#*^^ Pugcu/v^g. ' " -- - / -&J- JOB NO DRWG NO 1 REV. J----10095 DS-4--E-2. I ____________ L___ FORM H -IBB PART a 9 /6 6 WA-TEX 000793 7A PUMP DATA AND CURVES W&-TEX 000794 TABLE OF CONTENTS SECTION 7.k PUMP DATA AND CURVES Summary Table 7.l-l Data Sheets - All Pumps Pump Curves - All 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 |3--7/3 1-1/2 * Mech 3600 100 Mech Mech Motor Turbine Turbine Turbine Turbine WA-TEX 000796 ^ UR.WG6.5i CENTRIFUGAL PUMP DATA SHEET applicable io; proposals O furchaseo as sunt O NOTE <) INDICATES INFORMATION TO BE COMMUTED BY PURCHASER; jos no.A<$)Sl_jttM ud.A-R* Gi 5 G^KA PURCHASEORDERHO iS-OS =l. - & Q3L .. &>. Mawsmo* no........... .............. ... . INOUIBYHO...................... .............................. > . O BY MANUFACTURER . OATfREVISION________ . . TOO . \ sac. UNIT. C.KSApe. G-i>i.o/vM^trxwA _ <<a..'Ll<SALTs>. HD MIMAS RBr0__5L_ NO. MOTORS Rant \ ITEM N0.4d6d*-iL- PROVIDED BV--EAWtlfcilaMTD ST.JSr.AWfe.T . _LNO. TURIIMES RE0D- ITEM NO.PROVIDED BY_E^iitUJ'->Ci_MTO BY -EuXVfcT U4& PUMP MFB. AWrecr ..... SITE AMO TYPE g*1 RT~ A. A. SFRIAI ktt 1A A.2.5 OPERATING CONDITIONS, EACH PUMP U0U1B. V-TfertT WC -O.SSPM*|PT,NOB_ -RATED. -01SCH. PRESS. PSI6_ 11Z . ^ nr. f, nor.JJ&cE.max__ SUCT. PRESS, PSIGMAX- -BATED- SP OR. M PI--Q.5.<aA-------- OITT.PRESS,PSI- VAP. PRESS. M n. PSIA_2le___ OIEF. HEAD. IT WS.t PT. wJ2l?S..3.G_____ NPSHA, ft AO 7.8 CORR/ERDS. CAUSED BT_______________________ _HYO.HP A il CONSTRUCTION PERFOHMANCE PROPOSAL CURVE NO. `SIT b?OA.. BPM 352S NPSRR|WATER) fO BHP RATED MAX BHP RATED IMP T ___________ MAX HEAD RATED IMP I O MIN. CONTINUOUS fiPM *?, O ROTATION IVIEWEO FROM CP16 ENO| (`A'J SHOP TESTS NOZZLES SUCTION ' SIZE V" RATING "3,00 FACING Rf DISCHARGE ** 3oo RT A CASE-MOUNT: iSCEHTtRUNE OfOOT BRACKET D VERT. (TYPE|. SPLIT- AXIAL BRAD; TYPE V01UTE 0SGI QOBl O DIFFUSER PRESS: DMAS. AllOW--533-PSIS___OiCtt F: D HYDRO TEST LOCATION Ehib TOP -- .PSIE OW1T. PERF. DNON-WIT HV0B0 OWIT. HYORO OHPSH BEflO. OWIT. KPSH OSHOP INSPECTION O01SMAMT. AINSP. AFTER TEST QOTHEB. _ . ... -CONNECT: DVENT DFRA1N D6A6E IMPE11ER DUL: ORATED- &3/A- MODNT: OBETWEEN BROS pfOVEEHUNG ,, MAX- WttR.R&.OMM./CUWC.. TYPE:g^Sgjg MATERIALS 0EARINGSTYPE: nflABIAt ^iKlL. ... . OTHRUSTM=i__ API CASE/TRIM CLASSQ- LUBE RIMS Oil JS$FLOOO QOil MIST QFUNGER DPRESSURE Castt Cm,^. COUPIINS: QMBF_____ /?ALj g MODEL....S.:B4<---r^l 72&H/5L DRIVER HAlFMTO BY: OPUMPMFB O DRIVER MFR OPURCHASER Cav Tfcou jpspev.L.6 fe.. M 'VbtoCvt*. \rie Aft PACKING: O MFR & TYPE_____________ _____ ________ ___ DSIZE/NO. OF N8S_ MECR SEAL j^MFRAMnilfl /t&dAj/? /TZ AM Cl ASS CBM______ 'OMFBOCOE. . SJ-'"f.&S_______ --____________________ BASEPLATE: Q bfL VERTICAL PUMPS AUXILIARY PIPING OC.W.PIPE PLAN- -OCU-. OSS.; oTOBINS.- OPIPE- TOTAL CD0UN6WATER REDD. EPM___________ . O SIGHT FlREffO- FITOBSUMPOEPINO MIN. SUBMERGENCE BEQ'OD___ ................ COLUMN PIPE: RANGED ^THREADED OPACnNECOOUNS INJECTION REOC; Q TOTAL 6PM OPSG LINE SHAFT: OOPEN ENCLOSED OSEAt RUSH PIPE PUN.____ OtS. OSS OTUBING OPtPE- OEXTERNAt SEAL FLUSH FLUID- __________________ DSPM________ OAUXIUARY SEALPtAN_______ .OC.S. OSS. OTUBING OPm_ OAUX SEAL QUENCH FLUID- * fe.X\^T\ KJfS, MOTOR PBIVEB BR6S: DBOWl DUNE SHAFT OPSI6.----... BR6.LUBE DWATER POIL DGREASE otsfloat a rod Os.s. Obrz Onone ROAT SWITCH PUMP THRUST. LB DtiP- . DOOWN- JISfit. BPM 5600 .........G?.BEARINGS && HUME it VOLTS/PHASE/CYCLES .10----------------------------------- Full LOAD AMPS.___ /CL (ENC -- Xp________ TEMP RISE C~2L_10CXEQ KOTOR AMPS----------- :Q APPROXWT.PtlMPABASE- OVHS OVSS VERT. THRUST CAP, tS_ . SERVICE FACTOR- MOTOR .TURBIN AtPnIdSlWTAtNVDMARUDQ8ftVO GWOVERuNtSUvHn1EuS^S OMTIDLWgaIVWWISCEWNWOTEHOA.p^RAT^v-JXei J^.--. ^0^T,..4, I.t.--b' J . ...-I. ~ I X>^---.--lr--V.-V ^JpJg \ygMnQOg, oTfOlA QViQaml&m._Na &a ti tfMi ^Pa.i1*L! Ui v=*&a , KkiN iF*Kn ft ik\r_ c crvf# &^C0Mft>TlDK4& /jV P5ft- OhTk, HOT-SHOWN, Sb. -MSk/fiLJMu:te7 -- la-T.-t.-------- ---------------- JjS51 mp ? nftffc:, 4sr &U/A.r- /ssi/ex?/:<>&eS&AJsT'. / /ssuen ?=o te/J'Srguzrto^ r> 1 ssueo S=fR- auOTNTFOM NO OATF ... . JOB NO. DRAWING NO. | REV. m mncic I^ * SHEET-- .J -OF____ L___ WA-TEX 000797 m kwyf/NCj, pumps, job NotQDijSLiTEM Na.^B.6.Sr^.<afA CENTRIFUGAL PUMP DATA SHEET OAPPLICABIE TO: PROPOSALS PURCHASE O AS BUILT O NOTE. < J INDICATES INFORMATION TO BE COMPUTED BY PURCHASER- BY MANUFACTURE PURCHASE CROER HO._Z<22.7 & &/ BEOtNSITIONNO. .IQ.O. *}S T&.T.OS" 4 GI2 INQUIRY NO____________ ___ .. DATE_______ _____________ REVISION.... .................................... FOR -&AJWTAf&AOtOvk, (VyrUMir UNIT. SITE___I SOTiTf* ioi>ND JLIS80.1UIP. NO. PUMPS REO'DJ _NO. MOTORS RE0D_ LITEM NO.. _=______ PROVIDEO BY. NO. TURBINES RFirn ~-- -ITEM HO. ` PMVIDEOBY. PUMP MFR UUITlZh _____ SIZE AND TYPE___ (&a.`VTC> -MTDBY __ _MTO BY _ SERIAL NO. _74.4.2.7 /'I4426 A OPERATINQ CONDITIONS. EACH PUMP _____ -U.S.GPM*tPT.NOA_ .DISCR. PRESS. PSI6_____ PT. F. NOR.73S.MAX- . SUCT. PRESS. PSIB MAX. sp or it pt O.S7.3 -DIFF. PRESS. PSI________ VAP. PRESS. M PT. PSIA_.3i2.2_ . DIFF. HEAD, FI__________ vis. t pt. Sw-^C. 3.6--cp____ -NPSHA.FT_____________' CORR/EBOS. CAUSED BY..________ 3-2. L, NATta 78ld . JTL Ikg >3' DJPPe,7Z> _HYD. HP - A CONSTRUCTION PERFORMANCE proposal curve ko.-TJLz.323l rJkSL RPM /y-Sg^NPSHR|WATFBfflli.L(2^tS*'t MAX BHP RATED IMP________ SZ. G> ./SSL.MAX HEAD BATED 1MP_ MIN. CONTINUOUS GPM ROTATION (VIEWED FROM CPU END), SHOP TESTS NOZZLES SIZE RATING FACING LOCATION OWIT. PERF. SUCTION DISCHARGE 3" -ZOCr*^ *>>Ow er &. TOP ONPSH REO'O .TO/9_______ OW1T. HYDRO OWIT. NPSH ^CASE-MOUNT: &CEHTERLIHE OEOOT OBRACKET VERT.(TYPE) -SPLIT- Q AXIAL t^RAU: TYPE VOLUTE DSSt $BBl O DIFFUSER PRESS: DMAX ALLOW.. 4rOC> .PSI6 f_ F: D HYDRO TtST...Cg_CLO --PSIS O0ISMANT. & INSP. AFTER TEST OOTHER .. . CONNECT: 0vent Strain DBAGE IMPELLER DIA. DRATEO. _L"3_HuZik MOUNT. BETWEEN BRGS BOVERHUNG BEARINSS-TYPE: TKamhi PZALL LUBE: - b&ING OIL FLOOD OIL MIST MAX. WEAR RG. OIAM./CLRNC. FUNGER ^PRESSURE mvpfAasg/3 MATERIALS API CASE/TRIM CLASSO-- COUPLING: ffilJRF ________________ 0MODEL "SJ2/).C^r DRIVER HALF MTDBY: OPUMPMFR ODRIVERMFR O PURCHASER , PACKING: MFRSTYPEOSIZE/NO. OF RINGS. MECH. SEAL: MFR & ' API CUSS. CODE, BASEPLATE: . jSjAFROCOE____QP ~ />. /------ VERTICAL PUMPS AUXILIARY PIPING OtW. PIPE PLAN- .OCLfc O.S.S.: OTUWNS: OPJPE- TOTAL COOUN6 WATER REQD. GPM_ . O SIGHT El. ft0*D_ OPACKINS CODLING INJECTION RICO: DTOTAL GPM OPSIG OSEAl FLUSH PIPE PUN__________ OCR OS.S. OTUMG OPIPE, OEXTERNALSEAL FLUSH FLUID___________________ ____ DGPM________ Oauxiuaryseal plan______ .Ots. Oss. Otubing Op^e, QAUX SEAL QUENCH FLUID_ MOTOR DRIVER 1 Ah?S..<ZQ rpm. MFR... TYPE, }. ENC TPC. SAovhs OVSS TEMP RISE. C. VERT. THRUST CAP. IS. PStG, PIT OB SUMP DEPTHO MIN. SUBMERGENCE REffDD____ __________ __ COLUMN PIPE FLANGED THREADED LINE SHAFT: DOPEN ENCLOSED BRGS: DBOWl_______ LINE SHAFT____ BRG.LUBE OWATER OOll GREASE FLOAT & ROD LlC.S. OS.S. OSBZ ON0NE FLOAT SWITCH PUMP THRUST. LB O UP, . DOOWN, APPROX WT.PUMPA BASEMOTOR, 2 (> 7-1-73. IS3OBD. FOR CdbiST&QCTtQtJ I 7-2733 /ASUPUBtUfc&VS" 0 I 'A-T3. tS^ULSt) FPTt-QuQTftrzgw NO. DATE W JOB NO. DRAWING NO. REV. |DD<&S DS-4-G-3 2 SHEET_____i---------OF----- L WA-TEX 000798 t INM NO 130 IREVISEO APRIL 711 a5 w $ CENTRIFUGAL PUMP DATA SHEET APPLICABLE TO: PROPOSALS O PtffiCBASEO ASBUIUO job no.O.Q 3ST.item ho_4^B- II /A- PURCHASE ORDER NO.________ ______________ REQUISITION NO. .LOOj^ 5 * ' MOII. (.)INDICATES INFORMATION TO BE COMPLETED BY PURCHASER; a BY MANUFACTURER INQUIRY NO._________________ OATE_______ _____________REVISION... .. . . .. FOR xlsXAcAa- 3SE SITE. Ifo/.&gT iogUfeJB, UN!TfiA& ReCDv/gtty UNIT ...... smicE.&EBuWTK St \ TgO. pappy (,-7 . & NO. PUMPS REST). ITEM NO.UEiA.tL PROVIDEO BY-BiMP._fc?.MTD BY P.UMP MPG 7 & JTEM H04&dgUA PROVIDED BY^X&S&.'VO&MTDBY PERCHAiGfL- PUMP MED SI2E ANO TYPE ________________ .SERIAL HP/t /y?' A OPERATING CONDITIONS. EACH PUMP UQUID M.fe.HT___________ U S BMI mt PT, Him DISCH. PRESS. PSIG -Z1________________________ ______ FT P NOR .1/0 MAX............... SUCT. PRESS. PSIS MAX- . RATH) ' /L+*4- SP r.BaPl. 0.5?. (DFF.PftKS.KU 1 87 VAP. PRESS NPT.PSIA 15&Z-- 01FF.HFA0 FT... 730 . <3 VIS. M PT. StoXLJjQ--BF*-_____ -NPSHA.FT CORR/EROS. CAUSED BY... -HYD. HP^jQt.Q. PERFORMANCE LA-PROPOSAL CURVE NO___ ______ RPM_3515J- NPSHR (WATER) EFF..._5.&;g.BHP RATID_-^2. r MAX. BHP RATED IMP SP` >.. MAX. HEAD RATED IMP. MIN. CONTINUOUS 6PM UO ROTATION (VIEWED FROM CPLG N0| tCVKi KCONSTRUCTION SHOP TESTS NOZZLES SIZE RATING FA0N6 LOCATION SUCTION u_ ?DD R.F TOP DISCHARGE 2 3Dt R.P CASE-MOUNT: S&flENTERUNE OF00T BRACKET D VERT. ITTPE)_________ TOP -SPLIT: Q AXIAL f^RAO: TYPE VOtUTE DSSl $OBL DIFFUSER -PRESS: OMAX. ALLOW.. .SHQ.5__ PSIG __kP___ F: HYDRO TEST_JJt2P___ PStG LTNPSH REQ'O OWIT. PERF. '$#)l HYDRO OWIT. NPSH ODISMANT.RINSP AFTER TEST OOTHER . .. CONNECT: OVERT DFBAIN OGAGE IMPELLER BIA.: ORATED____ 1 O V^L OMAX.11x7______________ nTYPfcCLOSgD MOUNT: O BETWEEN BROS 0OVERHUNG O WEAR RG. 0IAM./C1RHC_______________ 31MATERIALS bearinbs-type: nradial .... BULL. OTHRUST_______________ BlkJSM. ARCASE/TWMCLASSO- LUBE: J&piNGDU FLOOD D OIL MIST FUNGER OPRESSURE -jGmiL-Prsj'ix COUPLING: OMHF FAiTT_____________ ________ nMnnn B ftEfcjA--E=iLk.l DRIVER HALF MTD BY: OPUMPMFR OORIVERMFR OPURCHASER CbyS -STEEL PACKING: D MFB & TYPEOSIZE/NO.OF RINGS. MECH. SEAL: n MFR A MODEL QQ__________ API CLASS. CODE- omfrocoE qa-lsoO 5D-7 N /gy OASEPlATE: O FS D.t?. VERTICAL PUMPS AUXILIARY PIPING Otw. PIPEPLAN_LE>_1 OCU; OS.S.; OTUBINB; OPIPE. TOTAL C00UN6WATER REDD. SPMOSIGHT F.L REQ'O OPACKINSCODUNG INJECTION REOTO: DTOTAIGPM OPSIG &0CKI?7 Li__T$j$SEAl FLUSH PIPE PLAN__ OCS. OS.& OTUBINB $MPF EVU. 80 ^11210 OEXTFRNAL SEAL FLUSH FLUID OSPM________________________________________________ OPSIG___ OAUXIUARY SEAL PLANOC-S. OSS. O TUBING OP"'E OAUX. SEAL QUENCH FLUIO_ HP /OP-- RPM 3bOO MFB--. A C. TYPE- A/QMt- mxiw ENC ___ TEMP Hist C MOTOR DRIVER /& FRAAIF ZfOffTA WIITS/fHASP/CYClES-4gl>0/&/fe O <3/?S,, ^ .FULL LOAD AMPS. gSHOCKED ROTOR AMPS OVHS QVSS VERT. THRUST CAP- US.SERVICE FACTOR- PIT OR SUMP BEPTRO MIN. SUBMERGENCE 000*0.0____ _________ __ COLUMN PIPE: FLANGED OTHREADEO LINE SHAFT: OOPEN O ENCLOSED BAGS; DBOWl___ DUNE SHAFT _.. .. BRB.IU8E OWATER OWL GREASE FLOAT A ROD OC.S. OSS QBRZ ON0NE FLOAT SWITCH PUMP THRUST. LB O UP- . ODOWN______ 9L*y fo.* APPROX. WT. PUMP & BASE, MOTOR. .TURBINE- inmnisD*inciwiieiiiiicnTttnNicMiRi WHLb VliKIT + tJYifTI lv) idfUM'SCJ'IUlji OaN ^yTA ff'.jmVC. &fepcw<6. H-'i/'73 m>iH4t73!/fs &&zr- /*st/r\f _&^xi;iTivS&'T>TR.g'\Mg_ TltLAKt W\i.u `-T7H- 2.6''Z. X. ?`U03 issvmi> pon. . TX* 1 1-2-7? ISW&D t=OVL XZQ-QlfO Tt? 7M*- 3 3-a-n CM 6' h AL?A_. - Mnz_ DRAVBIL. fi*. HO. DATE I \tj6 JOB NO. DRAWING NO. REV. ds-4-Gt-4 zooms' 1 SHEET-- t------- OF---------1_____ WA-TEX 000799 CENTRIFUGAL PUMP DATA SHEET AFPUCABLETO: PROPOSALS O PURCHASE O AS BUILT O NOTE: < J INDICATES INFORMATION TO BE COMPLETED BT PURCHASER; BY MANUFACTURER f- v ist t nc* r\\ m*' JOB MO tOO ^tS ITEM WO 4 & 50________ ORtC. PURCHASE ORDER NO..______ ______ ...... requisition no. WA.^7^>.F./ *a fW \ 1N0UIRY NO.___________ _________________ DATE_______ _____________ REVISION...................... FOR .JSkUNIT. Af Rgcoveay NO. PUMPS RED O. -NO. MOTORS REDD. _ITEM Ntt_ NO. TURBINES REQD___ IITEM NO AT pumpmfr fK>GI?R_<>OLt. - RkySfi Sin AND 1 SERVicE-A&SaB.eilO-hl_Ol.LjC k&K.G>i? pump PROVIDED BYMTDBY PROVIDED BV_Si&.1-l*t.MT0 BY e^.T3. tRIAlH0.)t>T2^S OPERATING CONDITIONS. EACH PUMP uauiO-AB SP tL P-Tl&ki____u.s. gpmupt. nor.rated. .Li 1ST --ttlJL------------------------------------- discs press, psie 5 ____ PI.F.NflB IQO MAX -SUCT. PRESS. PSIG MAX. .RATED. sp grpr___ P.TSg -DIFF. PRESS. PSt- VAP PRESS it PT.PSIA_liou.i_ OIFP. HEAD. FT_ VIS il PT. Sn_3ki^'_`SP>______NPSHA. Ft.. JJJaS. 1SL CORR/EROS. CAUSHIBV________________________ -HYD. HP I O S i *5 CONSTRUCTION PERFORMANCE PROPOSAL CURVE NO.JSLSJL^J. -. RPM *?>S ?C\ NPSHR |WATER)J>..y.Z.'. EFF- . 74/0. BHP RATED_\ A MAX BHP RATED IMP. MAX HEAD RATH! IMP 15 <aO MIN. CONTINUOUS GPM. ROTATION (VIEWED PROM CPLG END) C.C.V.I SHOP TESTS NOZZLES SIZE RATING FACING LOCATION OWIT. PERF. SUCTION AwJ.Rf . RP 5iDE OWIT. HYDRO DISCHARGE , Sl '/a.'4 ONPSHREO'D RE- _ %yn&_____ OSHOP INSPECTION OWIT. NPSH EASE-MOUNT; O CENTERLINE El FOOT BRACKET VERT. ITYPE)_____________ -SPLIT- ^ AXIAL RAO; TYPE VOLUTE OSSl DOBl DIFFUSER OfflSMANT. & INSP, AFTEH TEST PRESS. OMAX ALLOW.PSIGP; HYDRO TEST- -PSIG OOTHER . .. -CONNECT: VENT FRAIN DGAGE IMPOUROM.: ORATED. MOUNT: ^BETWEEN BRGS DOVERHUNG MAX WEAR. RG. OIAM./CLRHC.. orm.CiQSJ3 MATERIALS BEARINSS-TYPE aRADIAI OTHRUST_______________________________________ LUBE RING OIL FLOOD DILMIST OFUNGER PRESSURE COUPLING: I~1MBR S\jAL-T7feo AJ~UTAa&t.fTUr*i mmifi 3A- , ~ S^X ^fACCfc API CASE/TRIM CLASSO- DRIVER HALF MID BY: OPUMPMFR ODRIVER MFB OPURCHASER PACKING; MFRBTYPE_____________________ OS^Nd OF RINGSMECH. SEAL: QMFRB MODELAPI CUSS. CODE QMFROCOE. BASEPLATfc ^ VERTICAL PUMPS AUXILIARY PIPING OC.W. PIPEPIAN. -OCU: OSS: OTUBING; OPIPE. Q TOTAL COOUNS WATER REO'0,6PM. . OSISHT F.I. DEBT). OPACXING COOLING INJECTION REO'D: OTOTALGPM OPSIG OSEAl FLUSH PIPE PUN__________ OtS. OSS OTUBING OPIPE OaFERNAL SEAL FLUSH FLUID DOFM OAUXILIARYSEAL PLANOCX OSS. OTUBING OP"'E_ OAUX. SEAL QUENCH FLUID. PSI6. E XlSTWhMOTOB DRIVER-To Bl? f?*tOvl > pitorsumpdepihO MIN. SUBMERGENCE REQD.D------ -------------- ---- COLUMN PIPE: FLANGED QTNREADED LINE SHAFT; DOPEN ENCLOSED BAGS; OBOWL_______OUNE SHAFT _. . BRSLUBE QWATER OIL GREASE FLOATS BOD OCX OSS. CW OHOHE FLOAT SWITCH PUMP THRUST. IB UP. . DDOWN. Dim VuJr. V-z-ggrAjrA g Ows ovss API STANDARD BID GOVERNS UNLESS OTHERWISE NO^j-S---O--P--A---P : Q----P---l-^, --&1.t. TgQATr A ^c/D a.m 'L g>rA^E-t3 WfcMflllr t> o utoh* feZUfT~ /SW&D 0 Port. NO. DATE C&A/S7T GoaA&T/?FCTp*V, P 01 JOB NO. DRAWING NO. REV. iOOHS DS'4-G-ff O SHEET -t_ .OF-----1---------- WA-TEX 000800 CENTRIFUGAL PUMP DATA SHEET oapplicable ra proposalsO purchase as built O JMNoJQQg>S itemno 4B- o 30 A. PURCHASE ORDER N0._l.^Q'-\ S ~ GuO \ REQUISITION NO.. A. &.O S O\ NOTE. INDICATES INFORMATION TO BE COMPLETED BY PURCHASER: INQUIRY NO.___________ .... . . BY MANUFACTURE DATE--------------------------------REVISION.. . . FOR nzr UNIT. EECP&Efeji SERvictJAQ&OaPT(QM OM Cftkafrg NO. PUMPS RED'D__ I____ NO. MOTORS REDOITEM NO.. _____ ______________ _ . PROVIDED BY______ MTO BY__________________ NO. TURBINES REQ'D___ l ITEM No4ftE38A PROVIDED m fiTlTfelCh MTO BY .OT# lZ 2> PUMP MFR.JQTL Tfc.toA iSTfck r-.sc.sin AMD Hrtf-4- *.(&%!A sfmal mil _. OPERATING CONDITIONS. EACH PUMP UDUlD,,tLg>B.T. idbiJL.--U S GPU M PT. NRR US'L RATED SPQ. --OISCH. PRESS. F5I6_____ 384.___ ____ PT. F. N0a.iD.Q_.MAA. SPGRMPT- 0>~)b . SUCT. PRESS. PSIG MAX. *381-OIFF. PRESS. PSI_______ VAP. PRESS. PT. PSIA UllijL OIFF. HEAD. FT_ JJJaSL. VIS. PT. Sw_3..Q.g_CPNPSHA. FT____________ 10.1 _RATOJ_. CORR/EROS. CAUSED BY____________________________ _HYO. HP- CONSTRUCTION PERFORMANCE PROPOSAL ClllWt HD V- <o <V^> - TL RPM ^-50 HPSHRlWATER)_i?_........ MAX. BHP RATED IMP -3JL3_____________ MAX. HEAD RATED IMP t ~CO O MIK CONTINUOUS GPM 1 T- O ROTATION IVIEWED FROM CPLS EHD).&!*jL SHOP TESTS NOZZLES SIZE ' RATING FACING LOCATION OWIT. PERF. SUCTION DISCHARGE . . Aoo*- 4 O0 ToP T"O P L TNPSH REtrO |MBT HYDRO OWIT. NPSH CASE-MOUNT: JjCENTERtINE QfOOT BRACKET VERT.|TYPE|_ -SPUT- DAXIAt DRAD; TYPE VOLUTE OSBt J&.08L DIFFUSER -PRESS: OMAX.ALLOW,___eLL!5_PSIG___Jk Q-- f: HYDROTEST--L3=lO_0_ .PSIG .CONNECT- )VENT JlifRAlH OGAGE ODISMANT. & INSP. AFTER TEST OOTHER . . IMPELLER DIA. DBAtEn U7/S MOUNT: ^BETWEEN BRGS DOVERHUNG BFAR1NBS-TYPE: HRADIAL ^ALl MAX.. 13>V&- WEAR RG. DIAMyCIRNC.. QTYPE:Xio^Q MATERIALS nthrust T>R. API CASE/TRIM CLASSO- LUBE: ORWGOIl QflOOD OIL MIST HINDER PRESSURE COUPLING: PMRF FA^T____________ MODEL__l DRIVER HALF MTD BY; j&PUMP MFB jSfoBIVER MFR OPURCHASER CK&tg - STgISL. PACKING: H MFR A TYPE .' .. .. . . . OSIZE/ND. OF RINGS- MECH. SEAL: MFR A MODEL _yVyJ - R........ API Cl ASS CHOP SW P S O MFR 0C0E_____ Q Ps - -2- C-, S - 5 ~P . BASEPLATE: D . VERTICAL PUMPS AUXILIARY PIPING OCW.PIPEPUN^rg^SlOCU; OSS.; OTUBIHB: OPtPEy TOTAL COOUNSWATER REOU GPM .. OSIGHT F.L REDOI O'ACKIHS COOLING INJECTION RECTO: TOTAL GPM QPSIG OSEAl RUSH PIPE PUN-.X2-_.OtS OSS OTUIINS ftn>F $C.U $Q Soc* VOgc-g OEXTERNAl SEAL FLUSH FLUID QGPMOPSIG OAUXttlABY SEAL PLANQC.S. OS S. OTUBING OP"E- OAUX. SEAL QUENCH FLUID fiOEMLIA-C.OFAQ RrQO. MOTOR DRIVER PITOBSUMPDEPTHO___________ __________ MIN. SUBMERGENCE RID'D.O---------------------- --- COLUMN PIPE: FLANGED DTHHEAOEO LINE SHAFT- OPEN ENCLOSED BRGS: BOWL_______DUNE SHAFT _ BRG.IUBE DWATER OOIL Q GREASE UOATAROD OC.S. OSS CBR2 OHOHE FLOAT SWITCH ______________ PUMP THRUST. LB DUP_ . DDDWN- HP-- . RPM_ -FRAME- _VBLTS/PHASE/CYCtfS_ MFR.. -SEARINSSL. ___ LUBE_______________ TYPE--------ENC__ . g OVHS OVSS JBSUL- -FUUUMOAMPS- --TEMP RISE.C________ _10CKE0 ROTOR AMPS- VERT. THRUST CAP.Ul. . SERVICE FACTOR- APPBOX. WT. PUMP A BASE .'S.S.QQ____ MOTOR t4p/vtg - TURBINE Z.gfeQ ' S AM STANDARD BillGLWFRHSlLNIESSDTHFttWLSFIfflTFR 3 StlQg `DftWgft. AO Q|V*>UP\C?T>*L-- a ii/nfe &utP~ /$$az> e<s*Jsr; i 1`!S*BCF foft. tU+A.-.S? . o H-7-7Z /SSt/PD FOCI QUOT/x-TimJ NO. DATE W 585 w1 JOB NO. DRAWING NO. REV. I009Z DS-48-<} 1 SHEET L/.------ OF----- ---------- WA-TEX 000801 f CENTRIFUGAL PUMP DATA SHEET APWCMUTO. PROPOSALSO PURCHASEQ ASBUU.TO NOTE: O INDICATES INFORMATION TO BE COMPLETED BY PURCHASER: BY MANUFACTURER job mtOOSSitfu no *f&- GS&/.A PURCHASEORDERNO.___ :_____ __________________ RBBMSmON NO. JjO-O.^ *5. T _ -GCfcl \ .. . INQUIRY NO__________________ ..... . BATEREVISION... _............................. FOR sitf UNIT. /A/ IT SEovicE_ig/g4S./.7r7~^=v^ ux^P/zaiQUOT HO. PUMPS RHTO fZ NO. MOTORS REQ-D -- ITFM HO. ------;_____ PROVIDED BY ___ ____________MTU BY____________ _____________ NO. TURBINES REDD__ ,2_____ ITEM NOi..^^g%movroED by i^T*is7'/l*S_mo by _F~> & v-jp.. ., PUMP MfR_~>UAGAANA SITEAHOTYPE* 5X4 JLV\t^C6gSER>AlH0..22.S.^55/g335S<; A OPERATING CONDITIONS. EACH PUMP mma.4j&jbCT-jA_aA6<3s rpmi pt wir ' patwi O-zST PERFORMANCE PROPOSAL CURVE Mil <2>A -g>Q~7 pt.f.norj1S^_max - SltCTPflFSS.pSinM** (tiTFn SZ 3 RPM.&5&2_NPSHR IWATER|_LZ ." SP GR.1PT d>.G>Co VAP. PBESS.lt PI. PSIA ? VISmPT.Gm-^SP CP CORR/EROS. CAUSED BY.. BIFF. PfiFSS.. Ml OIFf. HFAfl FT HPSWLFT * //4 MAX. BHP RATED IMP 5*0 > ~Z. -4/2. MAX. HEAD RATED IMP 4-1? _ /_>__________________________________ MIN. CONTINUOUS GPM ) Qo -HYD. HP. ROTATION (VIEWED FROM CPLB END). (JcuT CONSTRUCTION SHOP TESTS NOZZLES SUCTION DISCHARGE SUE 4- 3 RATING 3 oo* 2*3 o'* FACING &C RF LOCATION EnSO ToP Owit. mt. J2&IT. HYDRO OWIT. NPSH SPLIT: D AXIAL ^fAB; TYPE VOLUTE ^61 DDBl DIFFUSER PRESS: OMAX ALLOW. ~2.___PSlG -_L5P_ F: P HYDRO TEST UQO CONNECT: OVENI &FRA1M OGAGF IMPELLER CIA.. nRATEIl I % <a| nMAT y l Vt- TYPE:iLk-JEj2. PSIG Odismant. a insp. after test Oother .. _____ _ . } MOUNT. DbEIWEENBRISS ^OVERHUNG riWFAB Rfi mAM/CIBNC PI MATERIALS BEARINGS-TYPE: DRAMAi J> A L. U ______________ nTHBUST'PgS'-Ro-O % A L, API CASE/7R1M ClASSO LUBE J2^8IMG OIL O FLOOD DOJI MIST OFUNGEB PRESSURE p-'Z/^y ... COUPLING: l~lMHF FAST MODEL: P-x/U DRIVER HALF MTO BY: OPUMPMFR OORIVER MFR ^PURCHASER - &Te-ETL. PACKING: MFR 8 TYPE DSUE/NO. OF RINGS. MECHSEAL: MFR8MnnEi -Q mtCIASS.rfltlF MFR new CP4-K.____________________________________________ BASEPLATE D . VERTICAL PUMPS AUXILIARY PIPING QCW. PIPE PUN. QCU: QS.S.: QTUBING: QPIPE- TOTAL C001IN6 WATER REDO. 6PM___________ O SIGHT FJ. REDO. OPAOUNECOOUNG INJECTION REaTk DT0TAL6PM DPSIS Oseal flush nn pun.__L2=. O cs. Oss Oturins owe. OEXTERNAISEAL FLUSH FLUID____________________ -- OGPM________ PSIG. OAUXIUABY SEAL PLANOCS. QS.S. OTUBIH0 OP"!E. CJAUX SEAL OUENCH FlUO. OQ&AJCtA C.QAJ A3EA.TKOit\ r*(vfyj lS> . T> HP______ . RPM_ MOTOR DRIVER .FRAME 7.VOITS/PHASE/CYCLES. MFR___________ ..BEARINGS. UIBE______________ TYPE___________ JNSttt. .FUlltOAOAMPS. ENC-- ----------- __ TEMP RISE C________ .LOCKED ROTOR AMPS. OVDS OVSS VERT.THRUST CAP. LB.. . SERVICE FACTOR- PIT0BSUMPDEPTHO MIN. SUBMERGENCE RED'D ____ ____________ COLUMN PIPE: Q FLANGED THREADED LINE SHAFT: Q OPEN PENCLOSED BR6S: BOWL_______ DUNE SHAFT, BBS.LUBE OWATER DOIl GREASE FE0AT8 ROD iXS. OS.S. OBRZ ONONE FLOAT SWITCH PUMP THRUST. LB OOP. . DDOWN. APPROX WT. PUMP 8 BASE. ..y.g.g MOTOR_____________ -TURBINE. AN STANDARD 610 GOVERNS UNLESS OTHERWISE NOTHL. FORM N O '1 3 0 1REVISED APRIL M l m A IM73 -is an/lP'-i'>s:un r&P poaJ&TS) I___ i__ 5 , 2 t o iokh? NO. DATE 4Wb iS&JD. DATA- tSS. feP CfirfSr. IsSOfe-O Ft>R-. Rl f.C.VV& CST;L> ifsSiJp C> OootaTi OpJ ...... Ja JOB NO. mt iUL id /oo$s 1 SHEET DRAWING NO. REV. 2 .OF--l------------ WA-TEX 000802 .......a - ^ OISl WA-TEX 000803 f WA-TEX 000804 I WA-TBX 000805 < mm WA-TEX 000806 ( WA-TEX 000807 I WA-TEX 000808 * k' * . * '% 7.5 instrument data 's*32feSsa{*a2s1eBssiaad 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 No. 4FE-100 4FE-105 Service Hvy Gasoline to 4B-C11 Abs. Oil Chg. Pump Orifice Size 2.596 1.600 TABLE 7.5-1 FLOW ELEMENT SUMMARY SHEET GAS RECOVERY UNIT PLANT ^B ANACORTES, WASHINGTON Line Size 4" Sch 40 3" Sch 40 He ter Coefficient 50 BPH 15 BPH WA-TEX 000812 Tag No. 4PSV-205 4PSV-20& ' _________ 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" 3/4" x I" 300 PSIG 75 PSIG WA-TEX 000813 >. WA-TEX 000814 ( FLUID INL1T flO MIN, QP6R* MAX, OUTLET.PSIG MIN, OPfR. MAX* INLET TEMP. F OPER. MAX. OPEfl. SP. GB. |`*i*Lpor MOL.WT. Th F er X FLASH OPER. WI*C.^XF. 31 |t)0 7M It uf (66 CfttT, PRESS. Pc OPEN. PLOW MIN. FLOW VAPOR PRPM^Pv SIZING PLOW MAX. PLOW 111. bX~l FLOW UNITS AP shut Off &P SIZING A P MIN. MfA m. \a ftp CvRSIZINGAPAFLOWl MIN. Cv -21 12*2 Cv-VALVE SELECTED FACTORS /L Kt6-.il m Too _2_ o.ib 2LC .221. lL SIZS PRESS. RATING MATERIAL SONNET TYPE packing lubricator TVPE CONNtCTlONS 3&01 8.F CLASS SOLTS TVPE I MATH. ISOL. VALVE $ >11. 1Sl Jtf3CL ica. 7sEr.o_x... SHUSH ISl ye* '/'SS Vj6>i. m *1- & CTO jtm -la, Vss fort size CHARAcren. GUIDE TYPE NO. OP PORTS PLUG TVPE TRIM SPEC. %3u FuOl BAL'D Ll&L CA&ff MhL *&?. fju. &a b til). CA<3& OfflWDit HMfcCrEmLMtt tootfl oftsu ACTUATOR TYPE !S MOTIVE POWER (LINEAR / ROTARY A4(L AiU. PRESS./VOLTAGE|P08. ON POWER PAIL COo^gl Ct.3%S d/a A. 4L L/fJ COObZ CU>-, MrAA, A/A. Ltu THRUST OR TORQUE RglfiHUT OPpfoPER ________ SIZE________ | MAX. OUTPUT HANUAL 0`RIOE|POS. FEEOSACXTYPE POSITIONER OUTPUT i SINGLE/OUAL . 4o 4o 3-\r INPUT SIGNAL BY-PASS SUPPLY PSIG GAUGES (hitter mto ^ frpgp M. ft. / f. O. NUMBER MANUFACTURER MODEL NO. P. & I. O. NUMBER SERVICE hA. - 4>> SlBsL. lr.\i J-4-M sfJiTinc f-rR:-24S Ja P.lJ.- _- tl.J -lg. caczfirtc) ee%* c. b*rrif Seises J- 4'l F.c-ffc. Uia7 t? C *lO eg. g a-/* -i u`UTt* tTR*r" 5g t/d Jrk7-{? J -OJ- 7 /.jgfl-p Asicf'iur Cn$ LINE SIZE - NO. SPEC INSTRUMENT TAG NO* 4"- ^o>n3 4 *>3* rj.pjd.ft, IF.--iOt 4LV- IQ IT*/ - 0,1 4Mr IB \Z_ . 1 ,0 iv*?S NO. DATE ORIGIN R&C ENG. CeVrS/OAJ l%(i0 P0L REVISIONS 14*46 tU*- .`j rr CONTROL VALVES JOS NO. : 3 DATA SHEET NUMBER REV. - J- >10 WA-TEX 000815 FLUID INLET PSIO Mitt. OPIB. max: outlet rsio MIN. OPCfl. MAX* INIET TEMP.F OPtR* MAX* OPEB. 81*. 6ft. j v**or MOL* WT, Tin F or * FLMH Open. VISC.(C.P. cmr.fAtts.fc VAPOR PRESSj#* TfT Si no hjL jjui 41 1.2. 3 174 JiCL 0.47' open* flow SIZING FLOW MIN. FLOW MAX. FLOW FLOW UNITS APStzmo &FSHUTOFF t F MIN. Cv SIZING a ft PLOW | MIN. Cv-VALVE SELECTED FACTORS PRESS. RATING material sonnet type TYPE CONNECTIONS class BOLTS TYPE 1 MATL 13l cm. 'loa v)S Cull 73. Z (" \uoae 3.0(3 1 Af IA`*> i>rc. ?>> _i_ IM M. ML K-.3 split &py S2DE /n*Ui> JtsL 9.H X**- . SL I 9e0* uSj. /* LUBRICATOR ISOL. VALVE .vAii/a ita--CHA iktfcz a" I 6acec 3ssc C,S, Pi AitJ -in2., -tes. 'Vc6 PORT SIZE CHARACTER, NO. OF FORTS PLUG TYPE fl/U. GUIDE TYPE TRIM SPEC, Action PUSH TP OF0H2.G3E row Ofwsctasts ACTUATOR TYPE **%&* ///MOTIVE POWER ILINEAR/ ROTARY PRESS./VOLTAGtlPOS. ON POWER PAIL (,1V. TOWKT OK TOESUE RBLjsHUT opp our. SIZE MAX. OUTPUT _2L UANUAL O'RIDE [POS. PEEPSACK TYPE POSITIONER OUTPUT ^ SINGLS/OUAL 3~rf INPUT SIGNAL SY-PASS SUPPLY PSI.O GAUGES IziL Yf5 to J12 Ml M. flWC- .Dtfftgfir, /CcO M.fbti. <ifTT -A- 3a. 3l l-tf flAL3Q(g i3L .t6g. w6pV5 t Oi*p. -&UL 1UJL ^L M. R./P.O. NUMBER MANUFACTURER MODEL NO. P. ft 1.0. NUMBER SERVICE jfia. .A - 4-u ..fr&Z JSE JalnOL X . ^7_.gS -CP-g 4 Rfr-I.C <r SEffjgSP*JT r*SA J> y~-LLt . t:c. H7 &0 4-CA-C, im *r* ->f= >-V --LJTrf..t-|._____ UNE SIZE-NO.-SPEC instrument tag no. 1LY--Ze>( 211 .H.fg 3 J?Z 5L Y-ZO? yLY- Zto * 4-* JO<a|3 iih.7?. i 1 VMi s 0 i-V-n $ NO. DATE ORIGIN R&C ENG. 6eu Cevi sioaj T^juso aoe PuteoMKe REVISIONS ftX.L-*Xp ' _____sy_ ST .4f1 r CONTROL VALVES r-CK y: JOB NO (00'4 J DATA SHEET NUMBER Ds - o - 1-1 REV. W&-TEX 000816 if 7.6 TRAY LOADINGS 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 10iK03 ttlB M T W ( t CiUOH TW3M30 "Io ^n3s^!ISnijnitv^_tS3Si<jijsa T WA-TEX 000819 ' WA-TEX 000820 Ti\iS/ ?'"-81 WA-TEX 000821 WA-TEX 000822 | WA-TEX 000823 T0*U HO. 0 * * . +* 0 * . I WA-TEX 000824 WA-TEX 000825 lull'sl S3 WA-TEX 000826 WA-TEX 000827 WA-TEX 000828 WA-TEX 000829 *C7 WA-TEX 000830 '*** I'X-ij --li -- iez <s/$'*-_ - 61 v-ii? -- i. \ixvct1 WA-TBX 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 2.5 23-8 1262 7-21 2.0 22.1 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