Document O5j73KnmawG4KXgMMk9Ow4YX
ADDENDUM TO THE OPERATING MANUAL
CATALYTIC POLYMERIZATION UNIT PLANT 5J
TEXACO INC. PUGET SOUND PLANT
ESTIMATE 3910
BECHTEL INCORPORATED HOUSTON, TEXAS 1973
I wa-TEX 000316
'*&<?$
(
1 TABLE OF CONTENTS !
A__________________________ J
\IA-TEX 000317
<
TABLE OF CONTENTS
1. General Description
.
A. Introduction
B. Basis of Design
C. Description of Additions and Modifications to the Unit
2. Control Features
A. Principal Control Features
3. Preparations for Operation
A. Startup Procedure
A. General
B. Recovery Section
6. Shutdown Procedures
9. Safety Features and Regulations
10. Appendix
10.1 Process and Utility Diagrams
10.2 Vessel Drawings
10.3 Heat Exchangers
.10.4 pumps
10.5 Instruments
. Page No.
l l 1
1 A 4 6 7 7 7 9 10
WA-TEX 000318
MgjHBffiaaag '. ^
1 GENERAL DESCRIPTION
1 WA-TEX 000319
, *f it
*
( GENERAL DESCRIPTION
A. INTRODUCTION
.
This addendum to the Operating Manual for the Catalytic Polyermfzation Unit at the Puget Sound Works of TEXACO Inc., Anacortes, Washington, covers the revamp of the Catalytic Polymerization Unit.. The principal new equipment for this revamp is:
Saturated C3-C4 Amine Treater
Saturated C3-C4 Caustic Treater
Saturated C3-C4 Regenerated Caustic Treater
Saturated C3-C4 Salt Filter
Propane Stripper
Attendant facilities for heat exchange, transfer of liquids, and control of operations.
B. BASIS OF DESIGN
General
In the feed preparation section, the revamp is limited to the cracked C3-C4 treater and the saturated C3-C4 treaters. The cracked C3-C4 treaters are to treat 7,9^3 BPSD of 03-04 from the Gas Recovery Unit. The saturated C3-C4 treaters are to treat a combined total of 7,017 BPSD of C3-C4 from the Crude Unit and the CRU.
In the recovery section, the revamp covers only the depropanizer. The de propanizer feed is the effluent from the saturated treaters in the feed preparation section. The condensed depropanizer overhead stream is fed to a new propane stripper from which 420 BPSD of propane product is recovered.
Process flow conditions for the revamped unit are shown on process flow diagrams 5-RA-l and 5-RA-2.
C. DESCRIPTION OF ADDITIONS AND MODIFICATIONS TO THE UNIT
This section describes only additions and significant modifications to the Catalytic Polymerization Unit. Reference should be made to the Operating Manual for the Catalytic Polymerization Unit for a descript ion'of the existing facilities.
%
WA-TEX 000320
I
Feed Preparation.Section (Reference PCID's 5-RA-** and 5-RA-25)
The cracked C3-C4 treaters are satisfactory, except that the 1-inch Raschig rings in the cracked C3-C11 water wash treater, 5J-C5, .are replaced with 2-inch Raschig rings.
Due to the higher feed rate, the saturated C3"Ci, treaters and salt filter are-replaced. The existing treaters are left in place and may be used as standby for the cracked treaters in the future, if tie-ins are provided. The saturated C3*C<, amine treater, 5J-C57, bas 23 sieve trays. The saturated C3-C4 caustic treater, 5J-C58, and the saturated C3-C4 regenerated caustic treater, 5J-C59, have packed beds of 2-inch carbon Raschig rings.
The saturated feed stream from the CRU and the Crude Unit flows in sequence through the saturated C3-C1, amine treater, 5J-C57, the saturated C^-C,, caustic treater, 5J-C58, the saturated C3-C1, regenerated caustic treater, 5J-C59, and the salt filter, 5J-C60. The treated stream flows through the depropanizer feed-bottoms exchanger, 5J-E57, to the cat. poly, depropan izer, 5J-C17-
Tie-ins are made at the suction and discharge lines of the amine charge pump, 5J-G6, and the rich amine charge line between the present amine regeneration unit and the new amine regeneration unit. These tie-ins will permit either unit or lean amine storage tank to be taken out of service for T&l. Each unit is capable of handling the total refinery MEA load when the FCCU is down and the CPU unsaturated treaters are out of service.
Recovery Section (Reference P6I0 5~RA-$)
The existing depropanizer, 5J-C17, is provided with a new feed-bottoms ex changer, 5J-E5I. A new depropanizer feed bypass pump, 5J-G62, is also provided that permits saturated C3-C1, from the feed preparation section to be pumped directly to CRU No. 2. The bottoms product from the depropanizer, 5J-C17, flows through the depropanizer feed-bottoms exchanger, 5J-E57, and the depropanizer bottoms copier, 5J"E59, to alkylation or storage. The cat. poly- debutanizer, 5J-C19, is not in service, since the Debutanizer in the atmospheric tower overhead section is in service.
Liquid overhead product from the depropanizer, 5J-CI7, is pumped from the
cat. poly, depropanizer accumulator, 5J-C18, to the propane .stripper, 5J-C61.
The propane stripper is packed with 30 feet of l-I/2-inch carbon steel pall
rings. Overhead vapor from the propane stripper, 5J-C6I, is combined with
vapor from the cat. poly, depropanizer accumulator, 5J-CI8, and the com
bined stream is sent to fuel gas. Alternately, the propane stripper overhead
vapor may be routed through the depropanizer condenser, 5J-EI3. Reboil
heat is supplied to the propane stripper, 5J-C61, in the propane stripper
reboiler, 5J-E58, by 1(0 lb. steam. Propane stripper bottoms product Is
cooled in the LPG cooler, 5J"El8, and sent to storage.
_
2 WA-TEX 000321
(
Utilities
Utility consumption by new or modified equipment is given In the following table:
I tern No.Service.
Consumption
Exhaust Steam
5J-E58
Propane Stripper Reboiler
585 Lb./Hr.
Cooling Water 5J-E59
Depropanizer Bottoms Cooler
.
146 GPM
Electrical 5J-G62 & G62A
Depropanizer Feed Bypass Pump & Spare
7.7 HP
3 WA-TEX 000322
* * rn^rn^-' i.
WA-TEX 000323
(
II- CONTROL FEATURES
A. PRINCIPAL CONTROL FEATURES
.
This section describes only additions and signlfcant modifications to the Catalytic Polymerization Unit controls. Reference should be made to the Operating Manual for the Catalytic Polymerization Unit for a description of existing controls.
Feed Preparation Section {Reference PSlD 5-RA-25)
The control scheme for the new saturated C3-.C4 treaters is the same as the control scheme for the existing saturated C3-C4 treaters. A description of the principal control features of the saturated C3-C4 feed preparation section follows.
The flow rates of saturated C3-C4 streams from the Crude Unit debutanizer and the Platformer debutanizer are controlled in their respective units. The combined saturated C3"C4 stream flows in sequence through the saturated C3-C4 amine treater, 5J-C57, the saturated C3-C4 caustic treater, 5J-C58, the saturated C3-C4 regenerated caustic treater, 5J-C59, and the saturated C3-C4 salt filter, 5J~C60. The treated stream passes through the depropan izer feed/bottoms exchanger, 5J-E57, to the cat. poly, depropanizer, 5J-C17. The pressure in the saturated C3-C4 treater section is set by the pressure in the cat. poly depropanizer, 5J~C17. Control of the cat., poly, depropanTzer pressure is described in the following section.
The flow rate of regenerated amine to the saturated C3-C4 amine treater, 5J-C57, is controlled by flow controller 5FIC-200,. The flow rate of spent amine from the bottom of the saturated C3-C4 amine treater is controlled by interface level controller 5LIC-201 to maintain an amine solution-hydro carbon interface in the top of the amine treater. High and low level alarms, 5LAH-201 and 5LAL-201, are provided for the amine solution-hydrocarbon interface.
Spent caustic is drained from the saturated C3-C4 caustic treater, 5J-C58, to spent caustic storage by manual control. The spent caustic is drained when the caustic-hydrocarbon interface appears in level glass 5LG-202. Care must be taken when draining the spent caustic to prevent hydrocarbons entering the spent caustic system. Fresh caustic and dilution water are charged to the saturated C3-C4 caustic treater, 5J-C58, by manual control. Fresh caustic is charged when the caustic-hydrocarbon interface appears in level glass
5LG-203.
The flow rate of regenerated caustic to the saturated C3-C4 regenerated caus tic treater, 5J-C59, is controlled by flow controller 5F1C-201. The flow
*
! WA-TEX 000324
(
rate of spent caustic from the bottom of the saturated C3-Ci, regenerated caustic treater is controlled by interface level controller, 5UC-205, to maintain a caustic-hydrocarbon interface in the top of the regenerated caustic treater. High and low level alarms, 5LAH-205 and 5LAL-205, are provided for the caustic-hydrocarbon Interface.
Water that accumulates in the bottom of the saturated C3-C4 salt filter is drained to the oily water sewer by manual control. The water-hydrocarbon interface may be observed in level glass LG-506.
Recovery Section (Reference P&ID 5"RA-5)
The amount of saturated C3--from the feed preparation section that is pumped directly to CRU No. 2 is controlled by flow controller 5FIC-205.
When the propane stripper, 5J-C61, is in operation, a vapor product will
be leaving the depropanizer-propane stripper system. For this case,
5HCV-6 and 5HC-20 should be positioned such that the depropanizer pressure
controller, 5PIC-106, positions control valve 5PIC-106VB to adjust vapor
flow from the system, and the cat..poly, depropanizer accumulator level
controller, 5LIC-I6, positions control valve 5PIC-I06VA to regulate cooling
water flow to the depropanizer condenser, 5J-E13. Feed to the propane
stripper will be regulated by flow controller 5FIC-207.
.
When the propane stripper, 5J-C61, is not in operation, an all liquid cat. poly, depropanizer overhead product may be obtained. For this case, 5HCV-6 should be positioned such that the depropanizer pressure controller, 5PIC-106, positions control valve 5PIC-106VA to adjust cooling water flow to the depropanizer condenser, 5J-E13, and the cat. poly, depropanizer accumulator level controller, 5LIC-49, resets the net product flow con troller, 5FIC-207. Noncondensibles may be vented from the system peri odically by operating hand controller 5HC-20 to open control valve 5PIC-106VB in the accumulator vapor line. A description of other controls on the cat. poly, depropanizer is given on page 21 of the Operating Manual for the Catalytic Polymerization Unit.
The temperature of the propane stripper bottoms is controlled by temperature controller 5TIC-205 that adjusts condensate discharge from the propane stripper reboiler, 5J-E58. Level in the bottom of the propane stripper, 5J-C61, is controlled by level control ler-5LIC-210 that adjusts discharge of LPG from the stripper.
5 , WA-TEX 000325
3. PREPARATION FOR STARTUP
WA-TEX 000326
(
111- PREPARATIONS FOR OPERATIONS ' Reference should be made to the Operating Manual for the Catalytic Polymeriza
tion Unit for a description of preparations for operations.
e
WA-TEX 000327
(
i A. STARTUP ` PR0CF0URES
WA-TEX 000328
i
IV - STARTUP PROCEDURE
A. GENERAL
Reference should be made to the Operating Manual for the Catalytic Polymer ization Unit for a description of the startup procedure for existing equip ment. The startup procedure for the new saturated C3-C4 treating section is similar to the startup procedure for the existing saturated C3-C4 treat ing section, and the existing procedure should be used.
B. RECOVERY SECTION
The cat. poly, depropanizer, 5J-C17, and its related equipment, can be started up by the procedure given in the Operating Manual for the Catalytic Polymerization Unit. The new depropanizer bottoms cooler, 5-1-E59, and the new depropanizer feed/bottoms exchanger, 5J-E57, are steam purged, tightnesstested, filled with fuel gas, and brought onstream in conjunction with the cat. poly- depropanizer.
The following procedure for startup of the propane stripper, 5-1-C61, and its related equipment, assumes that the cat. poly, depropanizer system is oper ating. The same procedure, with minor modifications, can be used for start up of the propane stripper in conjunction with startup of the cat. poly, depropanizer. An outline of the startup procedure is as follows:
1. Steam-purge for elimination of air.
2. Tightness-test and gas-fill.
3. Inventory and circulate to dry.
A. Adjust operating conditions.
Introduce steam through the steamout connection of the propane stripper and vent steam and air through the 2-inch vent at the top of the propane stripper. Permit the tubes of the propane stripper reboiler, 5J-E58, to fill with steam condensate,. When the propane stripper is thoroughly purged, as evidenced by a.strong show of steam from the vent, throttle the vent. Purge the propane stripper overhead line, 5J-0-219"3", to the block valve at line 6'`-5-1-0-45. Purge line 5J-0-220-3" to the block valve at line 4"-5J-0-l62.
NOTE: The propane stripper feed line, 5-1-0-225-3", and the propane Stripper
bottoms line, 5J-0-224-3", have been purged and placed in service. These
1`ines will contain hydrocarbons up to the block valves at the propane stripper
when the cat. poly, depropanizer is in service.
_
7 WA-TEX 000329
r\
I
Close the vent valve on the propane stripper and tightness-test at 25 pslg with steam. Drain steam condensate from all low point drains. After a successful tightness test, reduce the steam pressure to about 5 psig. Slowly pressurize the propane stripper by allowing cat. poly, depropanizer overhead vapors to enter the propane stripper through line 5J-0-2l9"3".
Drain steam condensate from all low point drains. Inventory the propane stripper with liquid from the cat. poly, depropanizer accumulator, 5J-C1B, through the propane stripper feed line. Commission the propane stripper reboiler, 5J-E58, and allow overhead vapor from the propane stripper to pass through the depropanizer condenser, 5J-E13, to the cat. poly, depro panizer accumulator, 5J-C18. Add inventory to the propane stripper as re quired. Continue operation in this manner until the propane stripper is free of water.
During the above propane stripper drying procedure, 5HCV-6 has been posi tioned such that the cat. poly, depropanizer pressure controller, 5PIC-106, regulates cooling water flow to the depropanizer condenser, and the cat. poly, depropanizer accumulator level controller, 5LIC-1*9, resets the net overhead product flow controller,.5FIC-207. The net liquid product passes through the LPG cooler, 5J-C20, to the chiller. After the propane stripper is dried, it may be brought onstream by the following steps:
1. Reroute propane stripper overhead vapor from the depropanizer condenser to the cat. poly, depropanizer accumulator vapor line, i)l,-5J-0-l62.
2. Reposition 5HCV-6 such that the cat. poly, depropanizer pres sure controller, 5PIC-106, regulates vapor flow from the cat. poly, depropanizer accumulator, and the cat. poly, depropan izer accumulator level controller, 5LIC-- , regulates cooling water flow to the depropanizer condenser, 5J-E13. Flow of net liquid from the cat. poly, depropanizer accumulator is regu lated by flow controller 5F1C-207.
3. Net liquid product from the cat. poly, depropanizer accumulator is rerouted from the LPG cooler, 5J-E18, to the propane stripper.
A. Bottoms product from the propane stripper is routed through the LPG cooler to the chiller. The propane stripper level controller, 5LIC-210, is put in service to regulate flow of propane stripper bottoms.
5. The propane stripper temperature controller, 5TIC-205, is put in service to regulate steam condensate flow from the propane stripper reboiler, 5J-E5.8.
8 WA-TEX 000330
6. SHUTDOWN : PROCEDURE
WA-TEX 000331
f
VI - SHUTDOWN PROCEDURES Reference should be made to the Operating Manual for the Catalytic Polymeriza tion Unit for a description of shutdown procedures for existing equipment. The shutdown procedure for the new saturated C3-C1, treating section is similar to the shutdown procedure for the existing saturated C3-C4 treating section, and the existing procedure-should be used. The propane stripper, 5J-C61, is shut down in conjunction with the cat. poly, depropanizer, 5J-C17, as follows:
1. Discontinue steam to the propane stripper reboHer, 5J-E58. 2. Pump out liquid products to storage as described in the Operating
Manual for the Catalytic Polymerization Unit. 3. Depressure the system to flare. h. Purge the system with steam to remove all hydrocarbon vapors
and vent to the atmosphere. Emergency shutdown procedures described in the Operating Manual for the Catalytic Polymerization Unit are applicable to the new saturated C3-C4 treating section and the propane stripper.
9
WA-TEX 000332
f
9. SAFETY FEATURES
,
& REGULATIONS i jnWxlifli ilTTT liinun-- i'_rf
I ! 1 !
WA-TEX 000333
IX - SAFETY FEATURES AMD REGULATIONS
Reference should be made to the Operating Manual for the Catalytic Polymerization Unit for a discussion of safety features and regulations.
The new relief valves installed are listed below:
Re I i e f Valve No.
_____________________ Service
5PSV-101
Saturated C3-C4 Amine Treater, 5J-C57
5PSV-102
Saturated C3-C|, Caustic Treater, 5J~C58
5PSV-103
Saturated C3"Ci, Regenerated Caustic Treater, 5J'C59
5PSV-10i(
Saturated C3_Ct, Salt Filter, 5J-C60
5PSV-105
Propane Stripper, 5J-C&1
All of the new relief valves discharge through the existing header system to the existing blowdown drum, 5J-C29. Bypass valves are provided around each of the new relief valves, so that the related equipment can be vented to the existing header system.
10
WA-TEX 000334
10. APPENDIX
l
V
WA-TEX 000335
( t '
10. Appendix 10.1 Process and Utility Diagrams 10.2 Vessel Drawings 10.3 Heat Exchangers 10.-4 Pump Data and Curves 10.5 Instruments
WA-TEX 000336
I
1 PROCESS & UTILITY' DIAGRAMS
| WA-TEX 000337
TABLE OF CONTENTS SECTION 10.1 PROCESS AND UTILITY 01AGRAMS
Process Flow Diagram Process Flow Diagram P&1D PS ID P&ID, Utility Plot Plan - CPU P&ID, Utility P&1D, Utility P&ID
Feed Preparation Section - CPU Recovery Section - CPU Feed Preparation Section - CPU Recovery Section - CPU Steam and Condensate Systems - CPU
Air and Blowdown System - CPU Water System - CPU Saturate Feed Preparation Section CPU
5'RA-I 5-RA-2 5-RA-it 5-RA-5 5-AA-7 5-AA-8 5-AA-IO 5-AA-l1
5-RA^25
WA-TEX 000338
'.M y n
V V V V W V V V IN
LE6EUD
PtPIMft SYMBOLS
IMSTRUMSW SYMPOLG
ntltr HOUHTE0
~SL TQAUSHmtR
*0100 MOUNTED
wive <omm`
Mtitutmtsoi utMt
jumtaEtuniiAi mo
<AmUAY TUttMQ
J---- vAMT NuMBt*
\TS/ IwWSilfTtPBMvNlWlwTl yr&v^tUbtBrictioi
IMSTRUMENT 1D6KITI FICATIOfJ ALL 'USTfluMlNt* MC LOPCD 1*1 ACCOOQAMCL WITH UVA. 0IAMOARDS tXCtPl A NOTto:*OA*UM3 RtlXKTS B*O*J0*IVA-
-
LIME IDEMTiCiCATIOKl rtt uufe wucftt mocite* i-jd Mtttutt mop mum bi auoum
--------
PHMJ0 IPtC.^
U Ml *----UUt MRJAt Ml b.e HutttiiJ) t-r-- comwwtv
> - tT. <0. PUU1 Uft
*09 UhtSl|*AiD FUAllt* kQt 010l't'*f6> PXtftME OkeP CILCtitATlOM t
fr-jo*nfo< -
I Cl, UP)H0 MlCINCATiOH ...*==- -- Mts _______________
pipimo specification
oo^0r4.
*'& <;o%q.auow.
TEXACO ST> 59J0
SYMBOLS
*|5TM&
NW
REMOVE RELOCATE NOT USED tt>0 NOT REMOVE)
DEMOTES Tlt-M NlMBtftS
r NOTES
L REVISIONS OF MAJOR 5Y5TEMS ARE DESIGNATED 0Y THE SYMBOLS SHOW# ABOVE. MINOR REVISIONS ARE CIRCLED AND INCLUDE A TRIANGULAR REVISION
Mark.
2. PIPING SERVICE SPECIFICATIONS FOR NtV/ UNCS ARE IM ACCORDANCE WITH GEMS J*2D8 TABLE 7.
3. UNE NUMBER 5UFFIXCS FOR INSOLATION
ARE IDENTIFIED AS FOLLOWS*
PP Ct A PHC
personnel protection COLO CONSERVATION PARTIAL HEAT CONSERVATION
~7~ FHC FULL HEAT CONSERVATION 4fik 0?C OPERATING TEMPERATURE CONTROL
ST STEAM TRACED
N1 HO INSULATION
) 4*to <fcp l**papA.gon *som emEftmo sti*** f CO\OfcNOA'E SYSTEM. ThC BAIL PiOVT 5UAM.
* BE SET TO SHUT OF* FOft WJiP OF SPECIFIC
] GRAVITY LESS Than WATER.
A5+YST*0fAe**T STSAM T^aOvuS *YMBOt-SS
m B-T2ACCD
.
..........
LINE IDENTIFICATION
rr T-6"7I3A-H! f t t------- insulation
teiAcoJ tixAco SIZt.
klQUIiHTS
PLANT. SUVKC
1 TEXACO FIFING MATEKIAL
nummk symiol Lnumu siKvict sncsncAtioH
a Ak
JO- Vb
<0*0 *110*5
J0*S?fe llO*a.f. COCKS,`Zip' <0t(R ALLOW.
0- fc> b S0QWg.& QAICS,`Ao COOft.iUOW. jo*`lib sooiif`cocKttv.o ccftg. auovT~ ;o for >}0* K.r. COCKS, w 0o.^ltow*
y
COMMODITY PEfrlSMATJ Qi|
CdwStNUA Mttlt
HW< felt IC < 5*1
iWM j HPt8W
j-t^nw.t.y owt %*ut 'mTh.p.
np^TUp.fciyrioo my
REFERENCE DRAWINGS
FKOCiSS>&!.&. CClO MCftMU CA1 POLY. UWlt
P0OCi0.Vt.p.rm^T0^,<|ttctf>otr yyf"
o'riurv* p&lp.*ieam 0 e&voiuSAit' system*
UTIUIV R 0LD.- XATEQ SVMlM*
UflUTY POTo '&! C tl0*00*U *rMJMS
0io.`TwKA6i tmttacoumcT<*j& um mta
0107 JUM-*CATAIVUQ MlVMiAttATlOU VUIT
$*RA*_4
lkA>fcJ Taa*t
ro 4,
NOT 6 5 V 5IM. lNaOiVI}lL 00075 TO *t -.M ACCOA0AMCI VifMDtfA $0>AI'I})
HA
*MK
ioe tww Lwl o.t* abo * p*5T| lUl BYPASS f PtV. IWH SJ-CI7 UM
3
** Pmv* 9lM|4>4*F lifX91
A ML*98
A 7VSt ioa kitrs au mi m & u>H-s
fel LX
& 1M1-S7 F4LlltoFklXSIUW5
CA
1 2M
jff
s
S3 Z5& vt*-d fU5fO> 04Y0ttP*`r<.J tMH ja' ~~n
Aw
3s
A bTO-jj ISSUtO eon JL00AOVAL An 1
itJ #+ g & n "iil sa m.
BECHTEL CORPORATION TAM KUKttKO
THE TEXAS COMPANY
PVOtr SOUND WORKS
PROCESS RlPlMO t, IUSTOUMCKJT DIAGRAM RECOVERY SECTIOSi
CATALYTIC POLYMCAlTATIOM UNIT
2523 5~RA~5(Kl
A
i'-'h
AbMO inEIRINSMT T5iU4 TPaeiH SYMBOLS ABNKn>
A
MJt
fiuouo YIC*|A
Lifif >S;,6^tT4 iTr V*L* tMO'O
rn.
ft Ttt Kr
A <!>hi
R&vibp PSSZ OSLMMNOi S.AArlOG RY.'ZA
m
A
Z-T-T3
RBV1SLO ft-AA*tOS
^ OOAyllHa RV. IA
Rp
H, REVISED PER ORAWIKG
\
5AA*I0S RSV.O___________
W- HVJtO FPA C^MSTCuCri^N
|tt
ItL* iff
1iit cUK
RM
1--
5fC
A % OPoweo iS Jlofe
" F
ISSUED FOR APPROVAL
*
C3FL V
MNM
CM* cy t*
-->
soil NOWt I MIMMS
MUM
BECHTEL
SSI TEXACO INC. SSSSa
moer sound flant
PROCESS PIPING INST. DIAGRAM RECOVERY SECTION
CATALYTIC POLMERIZATION UNIT
HUtlU WCM nxMirn- sM
5-RA-5
WA-TEX 000339
JO B %SZS G-RA-S-
JOB 2525 5-RA-4-
IMSTRUMENT TMfcOU
LOCAL. MOUNTED tt
w TRANSMITTER
DOAfiO MOUNTED
pftRssuae lime mblBVHINt AtKUHt
EUCTRICAL LEAD ---^..w i CAPILiAQV TUttMO
r---blANt UUHblfi /$TlY-|l)ifftUMSMT lOtUfJCICATION
tuLTPUMXUf UltHKI
-lus'nraHttmnrpiremo gt owttA
tMSTftUMEttr IDENTIFICATION
ALL .WMBVMtUTb AP( 0&t U1 ACCODDlUCe WlfH LS.A. ltluoaxos uettr as uotid: m un am* ro o*an* u-4
LIME INOEMTIPICATIOM
foa iut wMtfte vnocims aha tUCUUTIK
mop must se
-U.CO. HAUTHt
' DESIGNATED bt THE SVM60LS SHOWH A60VC. MIHOR REVISIONS ARE CIRCLED AND mCUIDE A. TRIAW#ytA,R REVISION
MARK. & PIPING SERVICE SPECIFICATIONS MR NEW
LINES ARE IM ACCORDANE WITH GEMS 4-204 TABLET.
3. LINE NUMBER SUFFIXES FOR INSOLATION
ARE IDENTIFIED AS FOLLOWS *
**
PP PERSONNEL PROTECTION CC COLO CONSERVATION
PHG PARTIAL NEAT CONSERVATION PNC FULL NEAT CONSERVATION OTC OPERATING ``EMPeftATVfie CONTROL
ST STEAM TRACED HO' ISOLATION
LINE IDENTIFICATION
JIAA---00--40322---6-MHS3AA-- Nl
|* * `
TEXACOJ TEXACO Sl2t I
-(H4UIATIOH XIOUIXEMENTS
: STMtoa^eg, 4flANT
NtIMUR
S*v<tf
I. rTEXACO PITINO MATERIAL
NUA*t{* SERVICE SPECirtCATION
A
FIPINfr SFEaFICVNOM
JC-Hb : ISO* APOAT&G '/,<?&**AUDV.
i &CO*ft F &AT8S 'A*tbMb AliM.
4CW-*tb I 0b*WOKBAtlU. '/ftbttt AllOtt.
*04t |
GATt&.W COftAALIGHT
j'o*S {|9<*tt.P. C6CKb.M*C0flB. AU9L
JP>*T3Qg*>.K SArefr, gona AiiowT*
40*06 I J09**.AC9CK. A^gfliWl.AtMOW.
COMMODITY PESIQNATIOM
4 UQITIC
PW pfioaos MITER
in la. 0
(0011116 VIA1IE
4T V
Mmeu&tMiut9)aw.
:7U NUMBEfllS
i56*UgPCS.6ATVALVE ^fa" ILF.
mtf4>C0MBlUS4TE IHTlCt MLTta
w 6 aooyuro cs. oatcwuie y,C
sax oa equal
&}* too
aOO*ttgp C.S.CATE VALVE ViCPX.OitiA53X6 OBEQUAL. jqo*rum cs. ckre valve w g-^.PAonc aso*toa equal 150* ft-<Vt> C. LUR-FLUO WIVE fojRJ.WttKCH OPEftATgO 3oo*n&o cs. u- plus vAivt V>bf. winch operated
MOTE*
S. Dtlmf*r MeAuAmtVAu0u1tV*(C*uI<-or*9UTi.W`7t. ** i **6*1j r 9IKMAAI.
t CthWt iU CiVLftC Uia (*MNfL6*>9l.*l6-t0t.Hb'4l< *0't4|l*O4A) r oomoogs to utmor aifcam trirw outu u.
^0T-TAHO>TW>tVbWUTWPTTm*AWft.W>TM
gtTEPgMCE PBAWIMSS PSO<kt>9 FC.P- QbCOVtB* 5>CT e*tPPL* W*T
pgpct C^tp,ggACTOQ5n CASPOW-uviif HTuirv P/I^.STU CCOmASvSTCwS. CAT. POLY vuir
UTILITY P/T.P. AIR ^QLOMTOwtl SY3TEM-CAIPQLY. UUlT giPCip Tam<A&fr/<MTfra4owMtcrm& uwfeS.OHy *t
2 Wnoarr.*uu -at pott omr utility ML0.wiTtfl.ar5ttNCitPPiYuuif
5^
^<|| < t/4
tee utrotemH0tWK*5tA>H la, rot UtOFOMU6t HE ftWS3fr>
rosLiororeev9Kow. $*tA4b*t
rU*l5JUM^iTa(r<*w ...... ..
>*-!> uir oOtO (2,47 liiUtD fOB APPROVAL
*3
Si
&ECBTCI CORPORATION
FAN nUNQSCO
THE TEXAS CQMPANT
WdSOUAWMlS
1
<434KI
PB0CES5 PJPIW& & IWSTRUMgW T DIAGRAM FEED PREPARATION 5t&TfOVJ `
CATALYTIC POLYMERIZATION OMIT
Pfc4Q0i-i-- s<< atmovioov sj tMi n>As j ft* 7.1-57
^
2525 5-RA-4 '>$,
Ift JOB Ms OIIIIO DWG N* ZZ2I3 SHT. Ma 05-t-O4
AW4Q rg ri.L.W,w+fa\j A 4)PULU7UO *ST' AA*>M WI'YT
A '<`k ATOSOST TO 5J*C*5>1*3*
A H. R5E*AVIAS*ElDOAPOTPDFRVA. WOING
p
#1 *%>d
A k:I55USO FOE CONbTAUCTlOM
A k*/,,
UrDATEO'R>Jo AMMO ISSUED FOR APPROVAL
_L__ tL
A OM "l TZ\*~
|SCAtt NOUF QIOUltB
SftAWt
BECHTEL
MOUSTOM
{texaco! TEXACO INC. [texagd
niCT SOUND PLANT
PROCESS PIPING $ INST. DIAGRAM
FEED PREPARATION SECTION
CATALYTIC POLYMERIZATION UNIT
1-
dj^ warn, took
lluaifl* 3079
5-RA-4II4-/S
WA-TEX 000340
NOTES
otttw **** or nncoviny 9c.ti **
a. 907* COMVSJUJoW ** VTYlt>J ANt **7 COWV**|OM 0F?noVltttt CHAUimO
*JMt CAT.P0t.Y- RtACTOS* . b. &5% HjOPAH*- MCOVfttfcY AT THE
- &MPL*MT.
* ....
2. 6UM JNMJSiTOR lit INJ5CTJO 0YTHC O** fltCpVEflruNrr ; 1NH<9>TDA iMJtCTtOH FACILITIES OFFPlat.
fQOCVM CaUDtpOMB wtw. REVt9tt> Ntf fP THCX
DfePftOPAmtR. THE MiettAi ftAL&MCfc m (5
FOft TOTM AVAH-AElt FdD. THE DCS WLL UaUDL*
AABOOtUoTUo`lOrt 'frroofFl T7<M3Tl**t.fTlfff8t0A. tCCKCHAA/CEOS AET ' the pPAuTAtjtxea wiu. not tt in jobation,
A
.EXHAUST STEAM
SYMBOLS
.11 / j- i .
EMStlMa NEW. REMOVE
A " A-A- A-A- relocate
------* No; utto OO Not REMOVE
'
RWtVWl*IiODUYM&0OOPL.M5 ASJHOOaMMU9AH6H0V&TkMZHtJPOIOfr.WCOfVM-EO
iSiOWS Ant C'CClE AMO nJctUOE A TeioUCU;
OfVtbJpN MMtt&.
1
-**'**'* >
Hatty* CCC.GJtSCUU* S70fcA <5tc Wit l)
-------------- 7-----------------------
REFEHEHCg DRAWINGS ?waii ft** frM.cntKWOT mut MWH ruVWAS.fQ PftlF. TtCT.,CT. POirUMlT
pmmnommg.fnKT tier, Amy
i23 nIJktvLt
>i>4 r t4
T
&pp9epW|2UooT
64QQ-->Z_
MM |mm
|nm rjiWo**.
eSCHTU CORPORATION wmwaKQ
"
THE TEXAS COMPANYmen sound wooes
&&
'i
POOCESS PLOW D1LS2LM UfcCOVfcRY SECY ION
CATALYTIC POLY-MfcSlZATlOH UNIT AMMO
ww 2525 5-Rft-2
.
itc 4a
WA-TEX 000341
U OTE.*
I. M04MAU CtU. 1% apllApUfe CASE VrfTH AtW RlAT* AJ MOAMAL CAPACITY*
1. ALffcftWAU. CASt \% OpttAtlMC CML WiJW CAT POWY PMUJOOWU.
(ft. LOuipMtMT OfcMOW I* AAitO OM MAXIMUM CAVt- COHPIJJOUV -IHOWU OH <VOW O/AALAM.
FIIUM* TIM* POB HATCH CAUSTIC TREATS*? IS *.l HM# IMAP 9NI06PM OP 15*61' CAUSTIC PLUS WATE8 or OICUriOM.
s: TAM colts paovioco \W Alt S7Aat ?ANX*. 6. 5M9 PlUUPtS M6ASU9A8 AT 60*P,
G.DM MIA(UID at OPAaAHHfc tftMPftaATum.
? *et nor! esuPwroiATEff?5. pooctos cokwoio vesfe o*v>at ouit for ccacjqeq
CyC+ AMO O*T0AY4O C%` C* WATERS 9 0A5CHI& SWG& OYQTHEaS.
ts 1
y
SYMBOLS U)
.............. CMATlUQ + pw MEM REMOVE
-A-fllW-yW- CEtOCATfi "<M> 0 0-0* MOT USED
PO MOT CXM0V5
> ftEVS-OV*, OP MAJOR SYSTEMS ART 015:CM4TC0 3Yfe StMOOCS SWOWljAftOvC . niVioa Divisionsaze aacuo t iucuiot a
^7tttAUCL PEVI5ION H*Pl.
*j
'CAA* hTt*M SfcEHOT
I"-|
/ t
/
L \
\ \ \
\
to tttrtXUY full &ASMIX DRUM
CAT POW SPMYTtA tHUTPOWM re csuo* pvawACt
PAOU AeftW.lfLV CAUSTIC SYATtM TO %**M1 CAUSTIC ST0AA01
X-- >
" 1""_....... ^--
TO VPG COO.ia <CAT.POLV-SHUT OOwmi
_
-r." - r,-
" 2^, ggs>
To CAT. Poly &4*Y09 3 Vfr ORl/M
_____ .,
SATURATES C>'C* TP CAT POUT 0PA0PAMti*'
\ \ TO WASTt WATUt DtSPOSAU
\ \TO AUCYLAUOtt
_y\
P-iAUPTTPm panma WVJ3flreXTTf KESSKEEB
I <ci a5l
Ki list MWtttl IT.*CO 6FM c Vt
-r i Il TIS
\jwlt
CASA NklMUl nrIMS Lilk I tIO own lAiTAITIASO
4H 6A 1 SO p i 90
V4 :*o I t*o
1>
REfEfiEKJCE PRAWIM55
PIKHi Slow DIAGRAM ncovtftv SLCIiON CAT pOVt UUlt 1 5-OA-t
PfiftCEso rvow*'j^.Pi4trroe*s^us*C'VA*stt*eovY im*t i 4-RA-t
puu cuw (uxb. ;eur. sect. ftiArroHmo unit
] A`A-T
mccso Plow 0M6*AM ALKVLAflOM UUIT
1 BA*1
p&ftcess ruoi1/ oiacaam w*vre wamu ososoAt.rccv i WVP
PReetlS rtftW OiaAAAM RIACTIOM SIC^CAT.TItYVUtr I 5*CA*5
WA-TEX 000342
.P9^CgUOaexg`AMOP5M.fetO
HLHICfCHJUcmcnwwittl u[ isauta fan Arpnov.t-
6400-
BECHTEl CORPORATION
MK HUHCttCO
THE TEXAS COMPANY
nxtn kmm& va
PROCESS FLOW DIAGRAM FEED PREPARATION SECTION CATALYTIC POLTMLEILATION UNIT
2525 5-RA-IJ3a
5} '1 jjj l | i
1 1
'y-V
flL
C5
cs
ca
G9
fcTT
led 4MI
|C!& few few
vwmu urw " cgicmocrci, caustic Tgtmtt G&GKLP Cfo~gCajflA7&P CiUSTfC 7BU!lEr
CgJLCKtP CvCi WASH WHU TEtATEg
0E61SSM6 DRUM SA1U2AHD 6rC ttME TgUTCR litmus crCt uustg cm_____________ AIU2ATL0 CfCc BEIitNUWto CAUSTIC TRUTtg
SlIUflATCO Cv Cfc SALT MPT caustic gtcojEgnott
CAUSTIC ttCtHeRMTOR ACCUMULATOR mui Bts&itgMoa. iMWCgCCBUEglTQg ACCUMULATOR CM PQIV tfuntt CAT POLY SPUTTER ACCUMULATOR fclT POLY OEPBOPAHUtt
CAT PQIV OtPnOPAWZttt ACCUMULATE CAT POLY OEBtfTAUtltg CATPOVY 08UTAM>ttg ACCMUIATM
12 MMawmojuBcerow*
rtEAtTOItS
WAivtT nutnT lew gucioa emuimt tush dbuvi
QUtijdH SCITU2 let? 0* CONg. nH gV3H
40 EOHR FIAVH QBUM
BlOWfrOWM OTgtP
CAUI7IC gt6t>f|gA7M SOMDIHIATC POT
AMIUE StORATOR CPUEroWATEPoT' SPUTICC CWOPttAU POT
KPgQPAKggg CMPlMSilE POT
OMUTAHKfg CCHQPHffl POT
KICTflgfno HflffU OMOmW* POT
KtACTCtt.ntO.vWlt*. 6TS
M.E.*. RCCtAIMBH _____________ gtCtUEBfllP ikMTft SIttAtt"7A&"
imi stegAO%lm ime tawT
tituoma tahx
f SB WHCMU6 TANK
ww&iroft frtey&wctAwtc
CAUSTIC BEGEHRATOft CWPEHSEtt
lT CAUSTIC UEO muz_____________________ tiwis BietHtiATOA ntftMTTQH uchamow"
liE B1CSMIBA1CP CAUSTIC CDOtEB
AHIKt COOlU
3hE gCSEUtgATPZ ft0-BOTTOMS &CMAHOB.
AMtt RtOlUMATCg CCMPWttCA
~
AIUI1L BISWIATOR gtgpTUft
|-gw<& CAT PCIY SPUTTER CWOfflMg
SPU77EB ftO0)U&
iPUTIjg FttO'BOnDMS WCHAHSgg
mw cat poly spurrer oonoMt cofrtu m PtPMPWfflig swamm
iwsr PEPQOPAmrcg fttnoata agsiffAUKia o.h. cpvomua OEBunmzu tam.1%
PQIV gAsoum ctoita"
l.RC, COOUt
EFTHlEUT CHASM ptcnmcit
PCCP HCATEB________ EfflUENT cwottHuT'
flash steam cna>mcL''
E1LTER AIP Mixing TAMX ,
aa WATER COAUCCER
HA FLASH RAT tMJLA. >VSTCU)
i f FPH'S SHO'L'N- OHINttOW* CtVtN Ifnon swk wt t t.cr fen's*
<
<
li
f1 lg*tryrwtMTdttlm>Tb8?.tOaAwMi-Tp9fl*uwIMeUmiCll
3
tsI Bill
1 fc.o ] ' cuoaivfr Ui'ia
uwtw .
MW S'A
s
en iL rf Si 'ill
vA
ffHJXTB rvrt* * OOkWJPVtuu W
tL *
`At ISSUED FOB tOrtSTRVtTIOM iil 1C
ccMAWHCAtitVPKP tOU AWIOVAL W )
wyrtrprng,itjmi
ni m
*.
sC3 as
i-!l *;!
g mu
nsUlB FOB A9M0VAI
IkkI
IITltlPM)
ai Ht 5 *yi <n ms m:
]
i
a
ite. h. n. ____
BKHTtt. CORPORATION
sutnweaeo
THE TEXAS COMPANY
fUGtr SOUHD WORKS
PLOT PLAN
CAT POW. UMIT
25251 5-AA-Sm
A
A1 Wu
1ST S)
5?
i 1 fK153060 TOtCCMSTOXtlOK
UNDATED *T0 JOB AWA*D
5H
tSSUCD rOHAFFROVAL
Pw a*
L---
*1 Ot(
IMv
tatt 1 Nftixia
MAva
BECHTEL
Houston
TEXACO INC.
ruoer sound flaw
@02
PLOT PLAN
CAT POLY. UNIT
tttrm* e*s mxttiri* 3f)0
5-AA-8 ISA
WA-TEX 000343 I
SgeiJd SYMBOLS
maa lyJMtiu8tIrtMsuUnUoufPMItt
A6M7 SYMBOLS
HPEUTIPICAtlOLl
I JPtHTfXlCATlOU t uuujua
IlMLMTmCATtOM'
.PIPlUft SIHC. CfttfHtll) . UUt USUI UUMMB . tixit C0.3WVIU KSisunou . PUUT UTUQCtneo.)
[- ouuruuuMaC^uum) |R- uut Ut*
*fiSl6imiOM ftlPOttVAPOa,FUEl.&A3 . ceeo w&rea ^ECiflCATIOtt c*uoj *uev.
|UE 16*-5J-C-Y06
pi
*a uui u'.iM.nr 4
jro
BECHTEL *10093
SYMBOLS
TEXACO ESt99J0
.y^-yr-ye-A-A A -
EXISTING
MErV
REMOVE
RELOCATE NOT USE fOO MOT REMOVE)
<3>
DENOTES T)E-m NUMBERS
MOTES
I. REVISIONS OF MAJOR SYSTEMS ARC DESICKA.U0 BY THE SrMEOtS SHOWN ABOVE. MINOR REGIONS APE CIRCLED AND INCLUDE A TRIAHCUIAR
REVlSiou MARC
1. PJPJN& SERVICE. SPECIFICATIONS FOR NEW LINES
are in accordance with Gtws
table 7.
3. UMe NUMBER SUFFIXES FOR INSULATION
ARE IDENTIFIED AS FOLLOWS * pp PERSONNEL PROTECTION
CC COLO CONSCRVATIOM *
*
PNC PARTIAL HEAT CONSERVATION FKC FULL HEAT CONSERVATION TC OPERATING TEMPERATURE COWr*L
ST STEAM TRACED Ml NO INSOLATION
`
Tine IDENTIFICATION
pB s,2t
NUMBER SYMBOL
Ml INSULATION ftEOUUEMCNl*
TEXACO PIPING MATERIAL SERVICE SPECIFICATION
a frk
*--k
5 'A A -IO
NT 4 IUCT.A9MP'6M mid
icr.cii pen. unit It.pou unit
ar. t78iY umt tCit.FOlt uuit 5P01Y. UUIT
BtLJtF L MOWOCWU
5DBfr 5-S1-6 3*U*7 5-U-ll
Tf------------- ---,--_j **
1| SADOft - /a U
90 jt v> 6 l at AH+VtAl
&A-H-4 f
***
O.L UM <
PC MM
Os.
toImyz
*P SP
ft
if*
F 2
tei
1______ m Oft EX WM SS
I E=.
A REVISED PER J3NXW1WO
it*'/# C-A.A..UQ ftFV. IA
A * "J! tREVISED PER ORAWNto S-AA'JIO REV.O _____
V
% jKiUUSD WL CON^TtUCTION oicWio'ko JoW
A H, 8ftSUEDF02 APPROVAL aMhM
TVS * OM
it Jtt
.fc lw M+
I HOME
BECHTEL
[COMPANY
Mo woks
rift
'O'
BUMtNT OliCCUM
PWU SYStSMS
?. UMIT
.
rflA-IQlXl/
II 7
SHT No 05-1-10
TEXACO INC.
PUOET SOUND PLANT
UTILITY PIPING 1 INSTRUMENT DIAGRAM AIR * BLOWDOWN SYSTEMS CAT. POLY. UNIT
Kecm- locos ttKMttn* 3019
5-AA-IO IA
WA-TEX 000344
IfitPIMO SYMBOLS
llivt
Mll UtltlTT MBTieu W'WNIR AMlt tiftftAU
.$&mo pnnc
VSt4
B iolmtCT
rifBE- WVOItAMT -
Trio
jjMfcUT lOEUTITlCAtlOU
r UUVtDtt flWUNT lOlWTIfKATiOrf ilUMftMT UUM&ia
g tOtHTIPICiriOXI
. piplltf iotc. (.DtCMttt) . cut M3UmvM*U . ICO'Wtttt
. 9tiur uttuui.t.co.)
. puui utmeu CMcnm) . L'Mt tUfc
~?VICS PESIQLMTIOBJ
j&yma Br*ct
^!lMO SPBCIFICATIOU &.. COfeROSIQH AtXQrtANCE
ganiXt.
W OOgPOSION ALlOiVAMCE
SECH7EL-10095
TEXACO EST.-SSIO
SYMBOLS
EXISTING MEW REMOVE RELOCATE MOT U6ED -4&0 NOT REMOVE)
OENOT&S TIE-IN NUMBERS
NOTES
I. REVISIONS OP MAJOR SYSTEMS ARE DESIGNATED
BY THE SYMBOLS SHOWN ABOVE. MINOR
REVISIONS ARE CiRCLtO AND INCLUDE A.
.
TRIANGULAR REVISION MARK.
t ft}PING SERVICE SPECIFICATIONS FOR NEW LINES ARE IN ACCORDANCE WITH GEMS j*m,tABte 7.
5. tINE NUMBER SUP FIXES FOR INSULATION OH NEW ARE IDENTIFIED AS FOLLOWS? P? PERSONNEL PROTECTION
CC COLD CONSERVATION
PNC PARTIAL HEAT CONSERVATION PNC FULL HEAT CONSERVATION
OTC OPERATING TEMPERATURE CONTROL
ST STEAM TRACED N| 0 INSULATION
. ^
A
LINE IDENTIFICATION
.... IIHK_. l jNUMecft
>~~ 6A"--.MJt?3A - N1
" SHI I
* -INSULATION UQOHiEMfNTS
Symbol -HUMBER
Texaco piping maiwai 'SEXVlCE SPECIFICATION
A
5-AA-H
fePENCE PPAWI1J65 fNUHouttctg<t.ftoit own
nntCTiOU-CiT.POtY.umt 3wee*u BY&nu-m pptY.uun
wa< cceuuc ano *yttM QlUOtMUM WHIM
|m rot. fltttlS AftCA
MOTfcS.
'CORMIAnOH
WimHmat
mISXAS COMPANY
ET tOUHD WORKS
|q < MSTflUMfcUT OUG8AM ATE* SYSTEM loLYMERIZATlON UNIT
5-AA-JI& n*"i
5
""
t+-n
RtVJSEO PR OAAWiMG S-AA-Ut RSV.O
3 ieoSO UTILITY ilADON
* MYDOAMT VAL.VESS
*P %
ST GP \T
pfjtVr $ t
I iDsuto tot. camzvcn&i
u SSm
A WMKI 1b&5*tMAjRD 1 ISSUED ftPZAPPEOVil
*
cST sl JT
- On*
I etscMto
j Or e**
bv. A-'-
BECHTEL
HOUSTON
TEXACO INC.
FUOET BOUND PLANT
UTJUTY PIPING* INSTRUMENT DIAGRAM WATER SYSTEM
CATALYTIC POLYMERIZATION UNIT
xtxm- MW* IttMNIT* mm
5-AA-ll 8SA
WA-TEX 000345
6ECMTCL - I0O9S
TEXACO EST. 59)0
5YM&OLS
Zlk
$
existing new Remove relocate NOTUSfcP-W>NOT EEMOVE DENOTES TIE-IN NUMBERS
Motes
REVISION OF MAJOR SYSTEMS ARE DESIGNATED
K>Y THE SYMBOLS SHOWN ABOVE. MINOR.
REVISIONS ARE CIRCLED AND INCLUDE A TRIANGULAR REVISION MAftR.
1. PIPING! SERVICE SPECIFICATIONS FOR NEW
LINES ARE IN ACCORDANCE WITH GEMS
j-aoe, TABLE 7.
.
3. LINE NUMBER SUFFIXES FOR INSULATION ARE
IDENTIFIEO AS FOLLOWS!
PP PERSONNEL PROTECTION
CC COLO CONSERVATION
PHC PARTIAL HEAT CONSERVATION
FHC FULL HEAT CONSERVATION
OTC OPERATING TEMPERATURE CONTROL
ST STEAM TRACED
1. . NO INSULATION
4 Imstrumemt steam tracws symbols*
! 0- Ttaocc-tO
/&.
I I THI- TgA.CEp4 HOOE&O
LINE IDENTIFICATION
IA-0-4M-6'-Jl,5A~Nl
rr rt
t-------- INSULATION
TEXACO-* TEXACO SIZE
requirements
punt
HUMBER
service
SYMBOL LN0MBEft
TEXACO PIPING MATERIAL 'SERVICE SPECIFICATION
.*McCnOvPfatTc*
KACQ]
f7z
|25~
lliX/li-titS ^pisL.BKI cj-Zdo
T? x>icsc*
ST&Ck*\
TRCACIK^ SYfAtiOt.5 A* fcK>Te>
p. 7ft
j<
A Wn
ADDED Ft&S TO
LJA SS-O-ZIbD
U T3_
A
plSUSTt?U * ST" 5*3- r- ?
$
P
A
zvn
.R.eVKi-0 PlTn. OvaG S-AA*l1s* 11PV. lb.
'
ft
W*\
or
A Hi REVISED PER DRAINING 5-AA-I25 REV.O
A issuto for CONSTRUCTION A
M*. OtM
ftwWtw
\
TBtl
ft if
> fcttj $
IT
n 21K. ir
*r
0*4
s**%
tMl|
b*. UfniL- AMR.
SCALE WPN& | DEStSHEO
DRAWN
BECHTEL HOUSTON
|fgc3l TEXACO INC. gexaco]
**^B&0**
PUGET SOUND PLANT
*^0*^
PROCE SS PIPING d INSTRUMENT DIAGRAM SAT FEED PREPARATION SECTION CATAI-YTIC POLYMERIZATION UNIT
MAN*. KCWIt- 10065 TEXACOIST- 3010
*.
5-RA-25 7A
i WA-TEX 000346
............ r
10.2 VESSEL DRAWINGS
A*iTB"*-r-annij 11 nse<BBaaaaga5ffif
WA-TEX 000347
{
TABLE OF CONTENTS SECTION 10.2 VESSEL DRAWINGS
Amine Treater Caustic Treater Regen. Caustic Treater Salt Fi1 ter Propane Stripper
5-DC-40 5-00-41 5-DC-42 5-DC-43 5-DC-44
WA-TEX 000348
WA-TEX 000349.
p\~%y.J
^
*? ; "
}*-- -- y ---
'1 ' . '
' "1
'
1
-
' '
" ............1
1
pyx 01 y y ^ 0 \/Sr
V jb V
1 ...........
"
1'
'
< ? ;-Zf "
_! '''T f* ? H
WA-TEX 000350
I
WA-TEX 000351
WA--TEX 000352'
VU P HA-SEX 000353
'<cjy
1
i
| i i f I i i
.10 ) HEAT EXCHANGERS
WA-TEX 000354
TABLE OF CONTENTS SECTION 10.3 HEAT EXCHANGERS
Summary Table 10.3. Data Sheets
Heat Exchangers Heat Exchangers
WA-TEX 000355
TABLE 10.3-1 EXCHANGER SUMMARY SHEET
CATALYTIC POLYMERIZATION UNIT PLANT Si
ANACORTES. WASHINGTON
i ATA________________________ _____________________ I ! Shell nata
1
No.
hi am.
1
Passes
I rtches
Material
No. Passes
f'ESIGN
Shell
Tube
Temp F
P res s PSIG
Temp F
Press PSIG
oof * \ oo
j2
15-1A
C.S.
1 650
650
300
1l 2
12
C.S.
1
400
65 200
275
jr' 6 19-1A C.S. 1 650
oO
150
lie
WA-TEX 000356
EXCHANGER SPECIFICATION SHEET
CUSTOMER AND PROJECT LOCATION
PLANT '
____
EXCHANGER NO ____
Texaco Imc. ... Py<UCT Sou MC_
Wr..sn
EXCHANGER
,,
mfr. Western Sopjpuv_
REO NO -Oa ITEM NO 3. " ~
''
EfRv.CE OP mt DepBOPANIHRFEP
s<?t IS K 24.Jp_______ . T.v AiS____________CONNECTED IN
SURFACE PER UNIT ^.73
^ SHELLS PER UNIT
\
SERIES SURFACE PER SHELL
parallel
" 4-73
EH *
F.UID
total
CIRCULATED Fluid ENTERING VAPOR................. Licuid ________
steam
performance
of one
UNIT
____ SHELL_ SIDE__________
TUBE SIDE
pkwa^J&fejiiac.R FtCD
_LRS/m ______&S,3S7_________
......
DE.PRQPAkHtHC.ft Btms. ______44,2.57__________________
.55- 3S1.
4-5, 2.57
non-condensibles
fluid VAPORIZED or condense?
b'FAM CONDFNSED
""
;R.*wiTv ; QUID viSE'-SiTy .'QUID
Sf
M.*-. rClll AR WEIGHT imm**
Cp
O.S4-LM - Q.49fetOoT> Q> 14- (In) ~ 0.1 &ut)
____ 5S.&`
Q.459Uh3-0.514 outT
6_.05.Cln > -6. It (Out)
5&.7.................................
1 .-i : .<f.at - L1O-.1O5
'
_ ____
u/m
a r u /*
. .-.'fA' <rA' - VAPORS
' * >.*! .'AT-iRE IN VIEHi'ilPE -'.ijT T'ERA'iNG PRESSURE
RUM:-fR -F PASSES
Vf
RI R| .'.HOP
26 " 27 r
V. RfSlSTANCE
Allow,' CALC MIN
___IQCL._ 154.
___ 2-4-5-
_______ 1_____
5 ~7~Z
8 T u /* *F f
FT /SEC W /SO IN
?s
154
23S 2 4- _
1.5 / 1.5
0.001
e u -
IT /Sf C
P SC IN
. -- -
28 J ...A- - -..A'iGFD - 0T-J /HR 29 f "!-;.Nr4 F P PATF ^FRVICE
>65QiOOO____
9a4. 9
CLEAN
M T 0 fCORRECTED) 4Co ACTuAl FOUt Nf F*crc
3D 1 * ,\ht pm v*/pf. 3* r .... -"OFSSURE
a 32 1
TtMPATURE
X 33 t * - B E s Camon
no t22
CONST R U C T 1 0 N
300 4-50 G56 0 D 8WG )4
*/S0 IN
3oo
*/SO IN
4SO
r ..., ufe5
Sflf .Ength 240* pitcn
1*
.-El. CA.R1QM &TCCL
p li '/A*
THICKNESS _ ________ _____________
#/ 50 N */> `N
a <jr *:
cover CAfttQM Steel
FLOATING Heto COVER CA.RBQH St eel
a-.vi CAlREOM Steel____________________
channel cover CkREON `iiTEFU _
fH SIMMS STATIONARY CkRftQU fSltoaetiengl CAnFEBOM StE-E-V-t'' -ROSS CarBOM StCCL. type SC.HCHTKU.>hickhess
EA Fl E
,,ONG
type
THfCXNCSS
IURL SUPPORTS
THlCKMeSS
IGASRFTS
VA6.TANL. Tacxeteo Kcbc<&to6
1 u>,f4!.cT`9NS_-: SHELL ~- IN
A*
OOUUTT
L*
I , THROSION ALLOWANCE -SHELL Side
OUT
T7 n--
[COCi REQUIREMENTS AL.5VAC. SEXTIOM VIIIDVtcna
class
RATING 300* RF
rating' 300* RP
tuc sior
iz&r
ft.SPEC
EtHT
WEIGHTS ~ EACH SHELL
_
OOTE 'NbiCATE AFTER EACH PART
Hr varus - EtS BA-ce-Lfi
BUNOLC
PULL OP WATER
WHETHER STRCSS RELIEVED IS R I AND WHETHER 5J/iT. BAkrpC.6-Cot. 23*4
RADIOGRAPHED l*-R> ----- -
tI>ItI
-A A
|A?(
V)5C.O. I4wldFr Cmt.
-i2u *n- [jaSOfeP Fog PvmCHAAC
TL* Z* TC-
JOB NO Rr; mo PEV 00)5 Bs-5-E-t^t
WA-TEX 000357
EXCHANGER SPECIFICATION SHEET
CUSTOMER AND
_
,
PROJECT LOCATION TE.'XA.C.O 1HC___________________
| PLANT
'
~~ PuCtT GoOHQ
- U EXCHANGER NO
ST- E69------------------------------------------------
* I SfRviCE or UNIT pcpRq.PA^Kn->P1R Bottoms Coouk
EXCHANGER
_
*FR.v/*fc-eH*.M " Supply
REO. NO E.-Q3 ___________
ITEM NO
5 Wt 19 24-0 ft surface per unit 'i4a
TTPE AES
CONNECTED IN
eft
SHELLS PER UNIT
\
SERIES SURFACE PER SHELL
parallel
Err
742. w
PERFORMANCE OF ONE UNIT
SHELL SIDE
TUBE SIDE
1 f 1UID CIRCULATED t 1 TOTAL FI UID ENTERING
OtPROP*>Vl.IR B*ri*5_
LSI**
49, 2S7
1] VAPOR LlCUiD
Ita STEAM NON-CONDENSIBLES
49, 2 51
....
Fl.uiD VAPORIZED or condensed t
STfAM CONOFNSED
GRAVITY-i :0UI0
J v*sr.TaT y vouo 1 M"i. f CUI AR WEIGHT - VAPORS
C,B.
0.514 Cl**1) - 0.554^Out1
.. O-U
0.145f0uT>
*1 <*'> iC "EAT - liODDS
j *.V*Vr
- VAPORS
T u/w # T O/W
Jj t f/t't A To RE IN
154 ............. f
' t V? t RATijPf GUT
IOO
V
C R A' VG PMFS5URE NUMBER -',r PASSES
PS*C
T250.........................................
VE: .--'r PR EsrviPf DROP
AiLOw/cALC
4/4
FT /SEC W /so IN
t ^ * t -V. P? SlSTAWCE
MIN 0.001
CoOUNC, V/AsTCR 73. OOO
73.000
74
. ...IOO
....... 40
G> 4,&4
12/1*2
0.003
mi/* B r u /+ F F
FT /SEC p/so IN
r ''.`"ANGCO - B T U / HR RATF - SFRViCE
1,750.000
7S.5
CLEAN
MTP ICORRECTED) ? 9 . a ACTUAL fOUl*NP r.*CTO
CONSTRUCT! 0 N
r: vc*> pesr>*-;Rt 5- npfGsuRE
DES'liN TEMPERATURE
500 450 450
*/S0 IN */S0 IN *F '
150
225
Sob
w/ SO IN P/SO m
33 res Ihh )saw
NO 1 9 ^ O 0 3/4 WG \Cw
34 l t M E 11 CA.REQN 5TECL
4-W
-EnGTh 24-0' THICKNESS
PI*GH I
JULk
33 "E - *. uover Carbon Steel
tloatinc heap cover carbon Steel
36 "A'inu Carson >thl
channel coe Carbon Stlel
3 5r i Tube SHEETS STATIONARY NKYA.U RaLLtD BRASS
floating KIkvAl. Rolllo B*ASS
0 38 r nAFF.ts - cross Carbon 5t&bl type se^me.mta.l.I'Ithickness
391 OAFFt E - ,_ON6
TVPC
thickness
40 1 TUBE SUPPORTS
THICKNESS
I4 f GASitfTs m&tal Jaeketeo _Av**ES*ro9
42 f CONNECTIONS-SHELL - IN
4
out
4H
RATING 300 *RF
43 |
-channel-in
4.*
OUT 4*
RATIN6 ISO RF
44 l< .-.ORPOSION ALLOWANCE-SHELL SIDE
->/&l>____ __ ______________ TUBE StOE
TTg"
43 u CODE REQUIREMENTS ASMC 5t.Tt<3t V It l Ck| TEAM CLASS
R
spec E.1 W")
46 t wfiGHTS - EACH SMELL
.
BUNDLE
FULL OF WATER
7
NOT INDICATE AfTt EACH PANT WHETHER STRESS ffELKVtD IS * > ANO WHETHER RAOIOCRAPHEO tl-A)
RtMARNS -m_BA.Pri.fc 5PALC1AHS
&*.PFL.C Cut. 10%
upitsU
A
<5ym5# &
-S"
: -/
, "
BCVi^p.0, l4oci> Fan Cou&t
h asutcy Rr PofcM*4e
'VC'
JOB NO drwg y BT
10095 * M
: REV j______ 1
WA-TEX 000358
EXCHANGER SPECIFICATION SHEET
y* CUSTOMER AND
PROJECT LOCATION
TevACO IkIC.
1 PLANT I l1 EXCHANGER no 4 ; I EfPv.CE CE UNIT
- rPu5cjTC-T cSSouind7 PROPKNC 5TRPRgR,,___
5 S.7E
TYPE /led
CONNECTED IN
6 SURFACE PER UNIT -95
^ SHELLS PER UNIT
|
EXCHANOER UFA. Hue.us.c -- A.NDeRSON
RED NO E-02
1TEM NO 13
SERIES SURFACE PER SHELL
parallfl
95 - Z
PERFORMANCE OF ONE SHELL SIJ>E_
UNIT ..................TUB E_ _S t OE
...............
? 'i>JiO CIRCULATED
_
TOTAL fi-i'O ENTERING
LS/>W
VAPOR
___ ^ ____ _
to
LICU>0
_____
_.
11 _
STfAM
___
12 JON-CONDENSIBLES
is n u .mo vttfooizEo Bwwerees
14 11.^VfAM (.ONI/f NSf D
3 t V.V/'** . OHIO
16 \ V, 'UiJiD
IT M- .*,!*. it* WEIGHT VALORS
16
*: *
A* t tOotOS
IS .- -*"f*rAT
20 f, t.*
- v-1
.i IN
'-..r
__
* F5IC
___ s as
PRo.etK.wt SiRjeetR Gtms
SOsO O
S5_ s as
Jiz i_..
. Md_.
9400
3^2 5"
JTT U/* T U/+
r
O. 4 <o 0.66? OmS - O-O^foor)
.. 4-3. a
B TU
_n2
e mj -
\\<k> 23 S
NUM:-- .* p.-.SSFS VE -t
:-Ri , ui ; HPf>
at low/calc
26 t' . . >** SiSTANCE
2T
min
_______ L
uo.
.
o-oobs
FT /SEC * /SO IH
.6.5. . / O S _ .0.601.
IT
* S- >N
26
Ft; BT-J -HO
340- OOP
MID (CORRECTED)
!;G>2 ..
29
11 or,T Sf RVICE
35. I
CLEAR
ACTUAL -foul.I*r T-CTOR
CONSTRUCTION
SO 'f.N .! V Pf
_CbS
27 S
5I
IOO
/so IN
32
MRIPATIJPE
400_____________
S3 " :F: l ' Caurdu Stcc-u NO *o o o 3/a* rffeojpRS'SS JEnGTh 72
34 r-Fl. Ck8on 5tEU.
i t>
_____12
tmicxncss
200
FlTCM
35 **s:. COVER CARt&oia StkCl-____________________________________ FLOATING hEAO cover
r * e.Q If* >/SQ
_____**_?
36 CAK&oR STJttk_____________________________________________ CHANNEL COVER CJkttfcOM STC C.
sr nfc VLMS STATION ART C/yttfeeVA STegV- _____________ FLOATING
38 (-tr uot,c' CkriioR `p-rsjtw.'Ssamceitku thickness
39 ! Jl f I l
.OSIG
_
_______ -_________ TYF.
THICKNC5S
O tuni SUPPORTS
.
thickness
41 askf TS mCTA.ll XkcKETED KiBgfi.TO&
~
____ .zZ iz42
l - <1(hHFEILL -- HINu
z>** "
OUT
1 I
RATING- ISO* R F
43 CHANNEL-in
OUT
RATING aOORF
r44
.45 46
iPPosioN t cwance -shell side
sTaT*-
ruse sior
C'jD! REQUIREMENTS A5MS. S6.CTIOT4 VMI PITCH* CLAW
r<lGxTS EACH SMELL
NOTE
-NtiCATE AT TEN
^
UNOLE
" FULL OF WATER
SPEC E.I rt7
EACH FART WHETHER STRESS RELIEVED S Rl AND WHETHER' RADIOGRAPHED C R
REMARKS -
51
!St5$
t*T|
L.\ m
-aL *P-p. [ISSUEOTottPutCMASg.
|*R.*
JOS NO* DRWG NC i REV
r,,
-m
f *
#6 100^5 ds-5-E-3( 1
>'** m Ifttf PAH*
,
WA-TEX 000359
10.*} PUMPS
< WA-TEX 000360
j. '
TABLE OF CONTENTS SECTION 10.A PUMPS Section 10.4 Pumps Summary Table 10.A.1 Data Sheets - All Pumps Pump Curves - All Pumps
( WA-TEX 000361
TABLE 10.4-1
CENTRIFUGAL PUMP SUMMARY SHEET
CATALYTIC POLYMERIZATION UNIT PLANT 5J ANACORTES, WASHINGTON
. CONSTRUCTION OATA
|I Impeller Di a.
Inches
iel ier
Raied
Max,
9 IO-IA
Nur.'ber Of
Stapes
Shaf t Seal
` RPH
DRIVER DATA
Rated H.P.
Type
Full Load Amps
9-1/2
10-1/2
Mech
3600
15
Mo to r
i
i, .
WA-TEX 000362
CENTRIFUGAL PUMP DATA SHEET
fe. st sx\ vac. Vu &
JOB NO U202>S. ITEM NO 5 S~. 5 " 3
PURCHASE OWE* NO j 9 O ^ 5 ~
--O
>Amicuuro proposal purchasejg( as iiwtO
) NOTE j INDICATES INFORMATION TO BE COMPUTED BY PURCHASER.
BY MANUFACTURER
JNEOWSmONNO 10O~}5~ 6* O'L
WORRY NO DATE .
REVISION
TM--- it*.AiQ.PhiL. ,,i:"~ se_
saws----------------
uwt
CkT PQLy
__________________________ service
NO PUMPS REVO i NO MOTOR* REOO_i____ITEM NO
PROVIDED BYlL>CkT'/ *^&MTODV
NO TURBINES REO O_n__ITEM NO -_____PROVIDED BY------------------ pumpmen VJLLSbNz - SNSfigp ________si7Fandtvw I`h ^7 1 ST&
MTU BY -- seriaino 4>S4\
OPERATING CONDITIONS. EACH PUMP
UQUID wktItPm
US CHBitW NOR IIP------ RAYED 1 3 `j __-I7
f\ f NOR 80 MAX
SPORitPT 1.0
VAP PRESS PY PSIA o
VIS MPT Sw CORR EROS CAUSEO BY
CP
OISCH PRESS. PSI6______ .3.PJ2 . ________ _
SUCT PRESS. PSIG MAX .
RATED 3 `S'
. ,,
m PRESS.PSI .
VL'L. ............... ..............
DIET HEAD FT NPSHA.FT ..
. ..
~7 3^
_______
.. . HYD HP .
................
__
%T.
CONSTRUCTION /t\
PERfORMANCE //\
HOPROPOSAL CURVE Z*)- l40-3DD
RPM 3550 NPSHR(WATER) U'/*
m BMP RATED MAX BMP RATED MNP 50. S %
MAX HUO RATED IMP
MIN CONTINUOUS GPM
..
ROTATION IVIEWED FROM CPIG ENDl
SHOP TESTS
NOTJLES
SIZE
RATING
FACING
SUCTION
"L
300
RF
mSCHAflbfc
. ill- -300_____ _JE______
/; USE MOUNT BCENTIRUNt OFDOT DIRACRET OVERT ITVPEI
SPIIT OAXIAt (!^1lAD TYPE VOLUTE pzfsGt 00*1 OOIFFUSER
press PImri auow
psis &'*' f Q(hydaotest
CONNECT ^VENT (S^FRAIN OGAGE
location
TOP TOP
G> PSIE
ynon wit .perf
twit perf
-non wit HYDRO
wit hydro
NPSH REO D
'WIT NPSH
SHOP INSPECTION
HHSMANT B INSP AFTER tfST
t 'OTHER
MCP".-
IMPEUER OIA ORATED B MOUNT QBETWEENBAGS J&Mtmim
) Gfhs- P-RfARINGS TYPE ORAOlAl
qmax
13
/LLi O type CU)yip4x
OWE** *0 OIAM.ORNC
MATERIALS
OTHRUST J3Add
API CASE TRlMCtASSO
imi
l USE SIRING Oil a HOOD Oil MIST OHINGER OPRESSURf
couPiiNG CSmrf
Dmobei
TTAdS.
GUOUP-
-cr
`
DRIVEA HALF MTD BY 'PUMP MFR ODRIVER MFR O PURCHASER
$WfcFT- M40U7
PACKING O MFR A TYPE
l. MECR SEAl (3-AIFRI MODEl
MFROCOE.
,
/&
.
SlZE/NO OF RINGS - . .API CUSS CODE..... _ ______
basepute q____.
._________
VERTICAL PUMPS
AUXILIARY PIPING
OCWPWPUN
. OCU. Css. OTUWNS. OPIPE .
________
O TOTAl COOLING WATER REQ'D DPMOSIGHT FI REDO____
. PACKING COWING INJECTION RED O OTDTAIGPV OPSIG
SEAIHUSH PIPE PIAN
..._l'CS OSS OTUBMG 1 TfIPE __________
IXTTRNAl SEAl HUSH HUID _______ .
, OGPM
_________ ..
I TauxuURY SEAl PUN
. i ICS ~ SS "sTUBING C P"E -
AU* SUl QUENCH HU10 ____ ___ .
________ __ __________________
OPSIG
MOTOR DRIVER
f^HP SO, MIR & i
\ TYPE
RPM S.LOC . ERAMEA44jl .VOUS/PHASE/CTUISJ
1EARINGS .d3AtU .. ___IUBE
lA/*0 INSUI _. -A .________ FUll LOAD AMPS
,4*t
inc / T C.
TEMP RISE. C $5*1 10CXED ROTOR AMPSr
isOvns -vss
VERT THRUST CAP. IB .._SERVICE FACTOR
JUO-
PIT OR SUMP DEPTHO-
MIN SUBMERGENCE REQ'O
COLUMN PIPE FUNDED OIHRIAOEO
LINE SHAFT OOPEN enclosed -
mss Qiowi
Dune shaft
BRG IUBE .OWATER OOU GREASE HOATBROO CS SS BRZ
NONE
HOAT SWlTCHO
PUMP THRUST IB O UP
O DOWN
AffWX WT fUMPKUSE
UOTOI
_ . - TURBINE .
API STANDARD BIO GOVERNS UNLESS OTHERWISE NOTED *=-X>~,TL yAC. FilFAP Mi'QlF'.EV Ssfc'licc. - NJS,vJ..-JjfrAl-
ua* ais iAIn 0(1 ON n a o i
? 1/IS/73 AS.BUfL.T- fSSVCD rG*e C.CUJST
1 it-4-71 i
noli puar.HjL ?a=
o u*"-T7
F^rt ounriiTioh* '
NO DATE
JOB NO .DRAWING NO REV
K u)k
Wk JT* Pi
J003S SHEET .
DS-5-&-2 /; . OF
1
WA-TEX 000363
m
o
)
CENTRIFUGAL PUMP DATA SHEET applicable io oproposals Opurchase Oas guilt
NOTE ,, INDICATES INFORMATION TO K COMPLETED GY PURCHASER. BY MANUFACTURER
mm/P% item no -4J'.rS <>'>
PURCHASE OROER NO__ .
MOWtmONNO .CO G
- (q l.
mournm. .
DATE-- . .
REVISION
x
/As<~
vr/^ />LY/ IrKt ZAJJQhL.
service.
NO MOTORS RBn>_2_ ITEM NO J-_ Q&Z/A PROVIDED VI-fv
ec_ ftEEG- Py*% / MTDBT fv*l r
NO TUMMOMOli-- ITEM NO =L----------PROVroCDBY.------------
.MfOiY
SB ANO TYPE 7 0)i25/0^A/<SjsrtSVi NO
OPERATING CONDITION. EACH PUMP
LIQUID *2/ -,S-
PT f NON /&O MAX
SP GR PT Ct 475
-1 U S 6PM M PT. NON
J^L-RATEO------
. _ nscN mss.rss____ 5 SLX--------------
--33(2suet press, psig max
-- rateo..
OIFF PRESS. PSI-
Z7.---------
Olff HEAD. FT______ 3 77` 5>.
VIS PT Sw
CP } NPSHA.fi .
-----------
CONI'ENDS CAUSED IT ________________ ____________ _________ HID HP
CONSTRUCTION
So
___________ PERFORMANCE
PROPOSAL CURVE NO '2424-7~~
RPM 355550 NPSHR (WATER! <* ^
75 sSEE 53357&.1t RATED , 3<kJ
MAX BHP RATED IMP . ./m
MAX HEAORATEOIMP
^kjQQ.
MIN CONTINUOUS GPM
TJS.
ROTATION (VIEWED FROM CPLOENO) CZC V\f
HOP TESTS
uNnOitEflES
NSOUCPTUIOMNPS HOD ~Z
OISCHARbf pump tu>
SIZE RATING
53oo* 7^2T 3oc&
FACING
split a axial jjjiuD type volute p(sa a on diffused mss Dma* Mom.(aCea7 psig (**& f Ohydro test
LOCATION
[NON-WIT PENT
7EN5D
'NON-WIT HYDRO
'NPSHREQO
___ ^SHOP INSPECTION
OWIT PERE ?LW1T HYDRO "'WIT NPSH
t smsmant a insp amen test
/(2dOrs& l HITHER
CONNECT |VENI l^frlfJRJAlIHN DOGpAAGl
IMPELLER oia nnateo
9 <72.
MOUNT BETWEEN RIGS SZbVERHUNG
^j
MAX /Cp -VL . ant*7J?SL
DWEAR R6 DIAM/ClItNC _.C?X i
MATERIALS
NfARINGS TYPE QRADIAL /\7*50>.35252/& 7-
O THRUST7ZjZ?~.`
z*5A API CASE-TRIM ClASSO
LUBE O RING OH DflOOO OOILMIST {STINGER PRESSURE
. F~
COUPLING DMRE
MODEL. --553
r -- -
' DRIVER HALF MTO BY JSfPUMP MER ODRIVER MER OPURCKASER
pacxing Date* t type . .
___ ____OSizi/M Of ring:
MECH SEAL MER A MODEL 7S 7\7~ 5053__ API^lSS J0I_
MEROCDE. _, .
. Cp g* Pr^fr1*
BASEPUTE VERTICAL PUMPS
AUXILIARY PIPING
PIT OR SUMP DEPTtO
I'veW PIPEPtAN --__OCU. OSS. OTURNS. OPIPt_________
n TOTAL COOLINGWATER RtOO GPM
02_________ OSGHTfl RED'D
MtH SUBMERGENCE REO D COLUMN PIPE OFIANGEO IHOEADFO
PACXING COOLING INJECTION RED'D TOTAL GPM QPSIG SUL ELUSH PIPE PLAN /^L-Jfcs OSS OTUWNG
_
LINE SHAFT DOPEN ENCLOSED
BUGS DBOWL
DUNE SHAFT
'flTENNAL SUL FLUSH ILUID ...___ _________ GPM ___ _
BAG LUBE WATER OtTIL GREASE
'AUXILIARY SUL HAN
. (ICS '`SS ''TUBING r-P-E...
FlOAT A ROD CS SS BRI HONE
AUX SUt OUENCHE1UID 'slATfcJU Q'||UGH CqaJ
FLOAT SWITCH
ITT?
PUMP THRUST 18 O UP
rzrMOTOR DRIVER
RPM i.ztpz&, zz.s__s___r__VOLTS/PHASE_/CYCLUj y/StJSFBl
DOWN
MIR A C5
.BUSINGS
LUBE. O `fcQ------------
TYPE /~7Cs </Z> -INSUt_____ 3 _.. _ FULL LOAD AMPS
.t
enc 7~55 SSZ uur*tsc_c53^7-- loatomwnum_________ /7 _____ M-
L'lVHS 'VSS
VERT THRUST CAP.TB ...SERVICE FACTOR
S, tg>
APPROX WT PUMPAMSt
-----
MOTOR 252. TURBINE..
API STANDARD BIO GOVERNS UNLESS OTHERWISE NOTED.
i 4SBuJLT-/5S<->>f&a C0AJS7?
\ ISSu&O PclZ 7ZUBCHA3& 0 1 t'lXMiLi can OooruriDij HO DATE
JOS NO DRAWING NO REV
\iT w (TX'BC
)
SHEET / - Of |
--
WA-TEX 000364
I
WA-TEX 000365
Byron w ckson
i
WA-TEX 000366
10,5 INSTRUMENTS
WA-TEX 000368
TABLE OF CONTENTS SECTION 10.5 - INSTRUMENTS
Summary Table - Flow Element Summary Table - Relief Valves Summary Table - Alarm and Shutdown Settings Control Valve Data Sheet
10.5.1 10.5.2 10.5.3
WA-TEX 000369
vn Ui Ui
I/o)<-T/J>(/*>D MOO
o *vi \n
HD0
O
yi VI VSI LA
TABLE 10.5-2
RELIEF VALVE SUHHAPV SHEET
TfA-TEX 000370-
1
I ls> -T"
ZZ
z Z Z TJ
Ul W VI U1 U1 UT
mln nmt *min nni7 mt itmi
N M M N M tO O OO O O O co '*o (a vn " o
VI
m*in
-- VO
o?2 - rot %o
"O TJ r* 13 -- m o. vn i
#TABLE 10.5-J, '
FLOW ELEMENT SUW1ARY SHEET CATALYTIC POLYMERIZATIOH UNIT PLANT 5J
ANACORTES. WASHINGTON
WA-TEX 000371
vwhoo vo--o. vvvoon w--ro wcno *vo*o>oi
w to w to to vw
(/> CD V) V> W U1 o o o o r o j 7y 7 y y Jr 4T Jr- Xr 4r
o --
--*
o o co co vn
!
oUloUloMHo
Ui W Vn Vi
fto Tto ThaTto ouiuiphp
inuuiu)
Vo Vo Vo Vo
U) UT Ul U1 VO V0 M '-J
*ti *a *d ra gggs
p sr+ ?rr.
P
(JHO* Q< p OSJ
" tH
r* <3 C tt
(<r9o <0h* Oo< <w
n
r** rnr
a or
o to NUlNUI iinp*- ps*
CO ^ co 4^
W 01 Cfl 01 o a>- l--I h-l I
qo
s _U|N S" rt
m * 00 !o-S ,,8mh23 tB)
So
ffB'B'S'
anna rt ft rr rr H H rt rt
IS i'rt rOt
WA-MOf 000372
4
CONTROL VALVE DATA SHEET
W&-TEX 000373
Jik.
FLUID
iNLrr.Ptta
OUTUT fIO
Ml* JOPCR.ImaK. MIN. OPiR, MAX.
SE
INLtT TfMf *F
}OPR.|max.
open, tr or 1"*^ J5TJT
T*h V f % FUAlH I OPEN. VlSC.*C.r.
UO h.
CWT. PACES. Ae VAPOR PRtSS^Pv
. ppca *low
MIN. PLOW PLOW UNIT*
H2INC PLOW MAX. PLOW P SIZING
iL Gf*\ n.06
A p shut off
Cv StZINO a p A PLOW I Cv-VALVE SELECTED
/HI
/ii.
PRESS. PATINO MATERIAL
BONNET TYPE
LOSRiCAtOR
/" I jct-zi
CONNECTIONS
$0#*\
BOLT* t j MAT'L*
tSOL. VALVC
sLL
KJ.H tKiXaTEtXPMT;
VcS I
brv.
y^5
m S$L
H3
110
ILL
2J2L
<7 _m_
JR.
9.&f
Ad.
x*-.8
spttr eu>-/
3
3E
ScjH
ar
PORT 3I2E CHARACTER.
NO. OP PORTS PLUOTYPi
fvu.
7.
QUIDS TYPE
TRIM SPEC.
TCTBJT PUtMTO
Om-CIQSE
FLOW: OPEMS-aOSES ci2JiJ
ACTUATOR TYPE
J*-I?//./-.
I A-.'i IMOTIVE POWER IlINEAR / ROTARY
PRESS/VOUTAOllpoS. ON POWER FAIL
THRUST 0* TBMUt KH (HUT OPpjoPSR,
SIZE
MAX. OUTPUT
kXANUAL O'RIOElPOt. FEEDBACK TYPE
JCL
POSITIONER OUTPUT I SINOlt/OUAL
INPUT BIOMAL
SUPPLY PSIO
BY-PASS
GAUGES
5->f
~K>
46#/
_2l. .for..
**<c~
JhL
JL
-lI
FORM NO.,
>ltQ
NO fifcTA
itnjg4
ii 1
3sdL
c.%.
jjJllV JiTCL.
ref.M
JfiL Vc9
nz:
.LdUi i6 a x- >f
iftP
Ain Liu
ZlL
^'jfcse-.T M. R./P.O. NUMBER MANUFACTUREB MODEL NO. P I.O. NUMBER SERVICE
ftfsi?.,
line size-no - spec. INSTRUMENT TAG NO.
J- 4-'t
finger.
662.. S
SPEtJl MSA
46.7...... 3..
4-Hit -tL
12SKZir'xrtu
faA<
4S3l
667 S
-r_A <r
j&.JLT-CA l___
r hia. LL12&
Lt v- te>i
5L V-tO? |-V - Zto
1-4-n
LSjit<W5
-Lh-7-D
4-ZA-C,
Tmo sri.
A
4-' )3ulQ
LLY-21.
t-*73
DATE
ORIGIN R*C ENQ.
&eu iBevi siofvj K^ugQ coiZ PjftirriM-e
fttVKKTN*
Tt>.A.C>T _____ __________
jsc.
a
CONTROL VALVES
P.Vii: Miift-c
4^wtel ...iftittS
XM ,
__
NO______ [00 Q 0
DATA SHEET NUMBER
DS - j - i^i
REV.
WA-?EX 000374
,,l
(' -
l
WA-TEX 000375