GE-103004, Other Liquid Transfer Pumps, P-104A&B
4
NOTE: PURCHASERS REFERENCES SITE CONDITIONS DESCRIPTION JO OPRNS ENGG PMT CERT E CENTRIFUGAL PUMP DATA SHEET FOR HORIZONTAL PUMPS AND VERTICAL IN-LINE PUMPS BY MANUFACTURER OF PUMPS OR PUMPS PER API-610 PERFORMANCE DATA BY MANUFACTURER OF PUMPS PER ASME B 73.1 OR B 73.2 O INDICATES INFORMATION TO BE COMPLETED BY PURCHASER; PUMP MFR APPLICABLE TO: SIZE & TYPE SERIAL NO. DRIVER TYPE ELECTRIC MOTOR THIS DATA SHEET COVER TWO(2) PUMP(S) PUMP MARK NO(S). P 104 A -G- -G- , -G- -G- , DRIVER DATA SHEET GEAR UNIT DATA SHEET N/A LUBE OIL SYST DATA SHEET N/A SAFETY INSTRUCTION SHEET SERVICE PUMP FUNCTION WASTE LIQUID PUMPS CONTINUOUS INTERMITTENT STANDY BY ATTENDED UNATTENDED INDIVIDUALLY IN SERIES IN PARALLEL UPSTREAM OF PUMP NO(S) -G- -G- DOWNSTREAM OF PUMP NO(S) -G- PUMPS OF IDENTICAL TYPE & SIZE IN OPERATION -G- -G- , -G- -G- , INDOOR OUTDOOR UNDER ROOF ON SHORE COASTAL OFF SHORE ELECTRICAL AREA CLASS , DIV. , GROUP PERFORMANCE RATED SPEED RPM DRIVER NAME PLATE POWER RATING HP RPM 120% PERFORMANCE AT TOTAL DIFF. HEAD EFFICIENCY REQUIRED POWER NPSH REQ'D FOR: 3% ΔΗ 1st STAGE ON H 2 O 40,000 HRS LIQ'D PUMPED Ft % HP Ft Ft SHUT-OFF HEAD AT ACTUAL IMP. DIAM. Ft AT MAX. IMP. DIAM. Ft CAPACITY AT END OF CURVE USGPM TOT.DIFF. HEAD AT END OF CURVE Ft RATIO. SHUT-OFF HEAD/RATED HEAD RATIO. END OF CURVE CAPACITY/RATED MINIMUM CONTINUOUS STABLE FLOW USGPM MINIMUM CONTINUOUS THERMAL FLOW USGPM OF RATED CAPACITY 100% MIN. CONT. STABLE FLOW PROPOSALS PURCHASE AS BUILT LCC EF $/kW NORMAL FLOW 00081 ISSUED FOR FINAL REVIEW SR DCO 104 B P BY: VISC. CORR. FACTOR C Q ; C H ; C E DATE: PROJECT ENGINEER CONSTRUCTION AGENCY SR 09-17-2011 1 f 4 00 GE‐103004 OPERATIONS CERTIFIED REV.NO. SHT.NO. DRAWING NO. DATA SHEET FOR DATE REV. NO. ENGINEER DISCIPLINE DATE: NM 09-17-2011 DATE: DCO 09-17-2011 DATE: DATE: DATE: CONSTRUCTION DATA -G- LIQUID CHARACTERISTICS LIQUID PUMPED WASTE LIQUID (Note 4) TDS PPM NORMAL FLOW TEMPERATURE 95 O F MAX. FLOW TEMPERATURE O F RELATIVE DENSITY AT NORMAL FLOW TEMP. 0.9 VISCOSITY AT FLOW TEMP. CS / CP / SSU VAPOR PRESSURE AT NORMAL FLOW TEMP. PSIA V.P. AT MAX. FLOW TEMP. PSIA TSS PPM NONE UNKNOWN CHARACTER OF SOLIDS: PULPY GRITTY HARD SOFT GAS IN FLUID: NONE VOL. % UNKNOWN PRINCIPAL CORROSIVES: pH CI PPM OPERATING CONDITIONS CAPACITY RATED USGPM RATED TOTAL DIFFERENTIAL HEAD 43.7 (13.3 m) Ft NPSH AVAILABLE AT SUCTION FLG. AT RATED CAPACITY 28 Ft AT 120% OF RATED CAPACITY Ft RATED SUCTION PRESSURE 12.52 PSIA MAX. SUCT. PR. AT RATED CAP. PSIA MAX. SUCT. PR. AT SHUT-OFF PSIA TOTAL DIFFERENTIAL PRESSURE 19 PSI RATED DISCHARGE PRESSURE 31.5 PSIA MAX. DISCH. PR. AT RATED CAP. PSIA MAXIMUM OPERATING TIME AT SHUT-OFF SEC FIRST CRIT. SPEED; DRY FIRST CRIT. SPEED; WET MAX. ALLOWABLE SPEED MAX. POWER FULL CURVE ACTUAL IMP.DIAM. POWER AT SHUT-OFF HEAD RPM RPM RPM HP HP PERFORMANCE WITH MAX. AND MIN. IMPELLER DIAMETERS MIN. MAX. TOT.DIFF. HEAD AT RATED CAPACITY EFFICIENCY AT RATED CAPACITY REQUIRED POWER AT RATED CAP. Ft MAX. REQUIRED POWER FULL CURVE % HP HP INTERMEDIATE TRANSMISSION RATIO GEAR BOX OF DRIVER SPEED HYDR. COUPL. SPEED RANGE % % PUMP TYPE HORIZONTAL (BET. BRGS) VERT. IN-LINE OVERHUNG INTEGRAL SHAFT CASING MOUNT: CENTERLINE FLANGE CENTERLINE FOOT VERT. IN-LINE IN-LINE CASE SUPPORTED CASING SPLIT AXIAL RADIAL CASING TYPE DOUBLE VOLUTE SINGLE VOLUTE DIFFUSOR STAGGER SELF PRIMING YES NO DIR. OF ROT. CCW CW (VIEWED FROM DRIVER) PUMP NOZZLES SUCTION LOCATION DISCHARGE FACING RATING SIZE END RF 150 TOP RF 150 / / 352 (80 M 3 /Hr) NORMAL USGPM CENTRIFUGAL PUMP A 9-17-20 1.2 176 1.45 25.7 1 of 4 00 Job No :
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Transcript of GE-103004, Other Liquid Transfer Pumps, P-104A&B
NOTE:
PURCHASERS REFERENCES SITE CONDITIONS
DESCRIP
TIO
NJO
OPR
NS
EN
GG
PMT
CERT
E
CENTRIFUGAL PUMP DATA SHEET FOR HORIZONTAL PUMPS AND VERTICAL IN-LINE PUMPS
BY MANUFACTURER OF PUMPS OR PUMPS PER API-610
PERFORMANCE DATA
BY MANUFACTURER OF PUMPS PER ASME B 73.1 OR B 73.2O INDICATES INFORMATION TO BE COMPLETED BY PURCHASER;
PUMP MFR
APPLICABLE TO:
SIZE & TYPESERIAL NO.
DRIVER TYPE ELECTRIC MOTORTHIS DATA SHEET COVER TWO(2) PUMP(S)PUMP MARK NO(S). P 104 A-G- -G-,
-G- -G-,
DRIVER DATA SHEETGEAR UNIT DATA SHEET N/ALUBE OIL SYST DATA SHEET N/ASAFETY INSTRUCTION SHEET
SERVICEPUMP FUNCTION WASTE LIQUID PUMPS
CONTINUOUS INTERMITTENT STANDY BY
ATTENDED UNATTENDED
INDIVIDUALLY IN SERIES IN PARALLEL
UPSTREAM OF PUMP NO(S) -G--G-
DOWNSTREAM OF PUMP NO(S) -G-
PUMPS OF IDENTICAL TYPE & SIZE IN OPERATION-G- -G-,-G- -G-,
INDOOR OUTDOOR UNDER ROOFON SHORE COASTAL OFF SHOREELECTRICAL AREA CLASS , DIV. , GROUP
PERFORMANCE
RATED SPEED RPMDRIVER NAME PLATE POWER RATING HP
RPM120%
PERFORMANCE AT
TOTAL DIFF. HEADEFFICIENCYREQUIRED POWERNPSH REQ'D FOR:3% ΔΗ 1st STAGE ON H2O40,000 HRS LIQ'D PUMPED
Ft%
HP
FtFt
SHUT-OFF HEAD AT ACTUAL IMP. DIAM. FtAT MAX. IMP. DIAM. FtCAPACITY AT END OF CURVE USGPMTOT.DIFF. HEAD AT END OF CURVE FtRATIO. SHUT-OFF HEAD/RATED HEADRATIO. END OF CURVE CAPACITY/RATED MINIMUM CONTINUOUS STABLE FLOW USGPMMINIMUM CONTINUOUS THERMAL FLOW USGPM
OF RATEDCAPACITY
100%MIN. CONT.STABLEFLOW
PROPOSALS PURCHASE AS BUILT
LCC EF $/kW
NORMALFLOW
0008
1IS
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FO
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104 BP
BY
: VISC. CORR. FACTOR CQ; CH; CE
DATE:
PROJECTENGINEER
CONSTRUCTIONAGENCY
SR
09-17-2011
1 f 4 00GE‐103004
OPERATIONS
CERTIFIED
REV.NO.SHT.NO.DRAWING NO.DATA SHEET FOR
DATE
REV.
NO
.
ENGINEERDISCIPLINE
DATE:
NM
09-17-2011
DATE:
DCO
09-17-2011
DATE:
DATE:
DA
TE:
CONSTRUCTION DATA
-G-
LIQUID CHARACTERISTICS
LIQUID PUMPED WASTE LIQUID (Note 4) TDS PPM
NORMAL FLOW TEMPERATURE 95OFMAX. FLOW TEMPERATURE OFRELATIVE DENSITY AT NORMAL FLOW TEMP. 0.9
VISCOSITY AT FLOW TEMP. CS / CP / SSU
VAPOR PRESSURE AT NORMAL
FLOW TEMP. PSIA
V.P. AT MAX. FLOW TEMP. PSIA
TSS PPMNONE UNKNOWN
CHARACTER OF SOLIDS: PULPY GRITTY HARD SOFT
GAS IN FLUID: NONE VOL. % UNKNOWN
PRINCIPAL CORROSIVES:
pH CI PPM
OPERATING CONDITIONS
CAPACITYRATED USGPM
RATED TOTAL DIFFERENTIAL HEAD 43.7 (13.3 m)FtNPSH AVAILABLE AT SUCTION FLG.
AT RATED CAPACITY 28Ft
AT 120% OF RATED CAPACITY Ft
RATED SUCTION PRESSURE 12.52PSIA
MAX. SUCT. PR. AT RATED CAP. PSIA
MAX. SUCT. PR. AT SHUT-OFF PSIA
TOTAL DIFFERENTIAL PRESSURE 19PSI
RATED DISCHARGE PRESSURE 31.5PSIA
MAX. DISCH. PR. AT RATED CAP. PSIA
MAXIMUM OPERATING TIME AT SHUT-OFF SECFIRST CRIT. SPEED; DRYFIRST CRIT. SPEED; WETMAX. ALLOWABLE SPEEDMAX. POWER FULL CURVE ACTUAL IMP.DIAM.POWER AT SHUT-OFF HEAD
RPMRPMRPM
HPHP
PERFORMANCE WITH MAX. ANDMIN. IMPELLER DIAMETERS
MIN.MAX.TOT.DIFF. HEAD AT RATED CAPACITYEFFICIENCY AT RATED CAPACITYREQUIRED POWER AT RATED CAP.
Ft
MAX. REQUIRED POWER FULL CURVE
%HPHP
INTERMEDIATE TRANSMISSIONRATIOGEAR BOX
OF DRIVER SPEEDHYDR. COUPL. SPEED RANGE %%
PUMP TYPEHORIZONTAL (BET. BRGS)VERT. IN-LINE
OVERHUNGINTEGRAL SHAFT
CASING MOUNT: CENTERLINE FLANGE CENTERLINEFOOT
VERT. IN-LINE IN-LINE CASE SUPPORTEDCASING SPLIT AXIAL RADIALCASING TYPE DOUBLE VOLUTE SINGLE VOLUTE
DIFFUSOR STAGGERSELF PRIMING YES NODIR. OF ROT. CCW CW(VIEWED FROM DRIVER)
PUMP NOZZLES
SUCTIONLOCATION
DISCHARGE
FACINGRATINGSIZEENDRF150TOPRF150
/
/
352 (80 M3/Hr)NORMAL USGPM
CENTRIFUGAL PUMP
A9-
17-2
0
1.2
176
1.45
25.7
1 of 4 00JOJob No :
NOTE:
CONSTRUCTION DATA (CONT'D) CONSTRUCTION DATA (CONT'D)
DESCRIP
TIO
NO
PRN
SEN
GG
PMT
CERT
E
CENTRIFUGAL PUMP DATA SHEET FOR HORIZONTAL PUMPS AND VERTICAL IN-LINE PUMPS
BY MANUFACTURER OF PUMPS OR PUMPS PER API 610
BY MANUFACTURER OF PUMPS PER ASME B 73.1 OR B 73.2O INDICATES INFORMATION TO BE COMPLETED BY PURCHASER;
Δ/ ALLOWABLE FORCES AND MOMENTS
FORCES AND MOMENTS
TOP NOZZLE SIDE NOZZLE END NOZZLE EACH NOZZLE
Fx LB Fx LB Fx LB Mx LB.FT
Fy LB Fy LB Fy LB My LB.FT
Fz LB Fz LB Fz LB Mz LB.FT
MISC CONNECTIONS TYPESIZEQTY.LUBE OIL INLETLUBE OIL OUTLETSEAL LIQUID INLETSEAL LIQUID DRAINCASING DRAIN(S)VENTSCOOLING WATERSTUFFING BOXBALANCE DRUMDRAIN & VENT INDIVIDUALLY PIPED WITH BLOCK VALVES TO TERMINATEAT EDGE OF BASE PLATE IN COMMON AREAFLANGE RATING in CLASS
YESO NOO
PRESSURES
HYDROST.TEST PRESS.
Δ/
CASE
MAX. ALLOW.WORK. PRESS.
AT OF
JACKETS COILS
PSIGPSIGPSIG
PRESSURES
ININSIDE DIAMETER
STUFFING BOX DATAINBOARD / OUTBORAD
Δ/
INDEPTHDISTANCE FACE OF STUFFING BOX
INFLANGE TO NEAREST OBSTRUCTION
NUMBER OF STAGESFOLLOWSTAGE
IMPELLER DATA
ACTUAL DIAMETER IN
FIRSTSTAGE
Δ/ MAXIMUM DIAMETER INΔ/ MINIMUM DIAMETER IN
SINGLE / DOUBLE SUCTIONΔ/ EYE AREA IMPELLER SQ.IN
VANE ANGLE AT IMP. EXIT O
Δ/ NUMBER OF VANESACTUAL PERIPHERAL SPEED FT/S
MAX.ALLOW.PERIPH.SP'D AT FLOW TEMP. FT/S
PATTERN NUMBERPRECISION CAST YES - NO
Δ/ CUT WATER DIAMETER IN
SPECIFIC SPEEDSUCTION SPECIFIC SPEED AT 3% ΔH
Δ/
O/
Δ/
0008
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DATE:
PROJECTENGINEER
CONSTRUCTIONAGENCY
SR
2 f 4 00
OPERATIONS
CERTIFIED
REV.NO.SHT.NO.DRAWING NO.DATA SHEET FOR
DATE
REV.
NO
.
ENGINEERDISCIPLINE
DATE:
DATE:
DCO
DATE:
DATE:
DUAL MECH.SEAL PSIG
SHAFT DATAINSHAFT DIAMETER AT MECH. SEAL SLEEVEINSHAFT DIAMETER AT BEARINGSINSHAFT DIAMETER AT 1ST STAGE IMPELLERINBEARING SPANINSTATIC SHAFT DEFLECTION
SHAFT SEALINGPACKED STUFFING BOX PACKING MAT'L. (Note 3)OPROVIDED WITH LANTERN RING: YESO NOOSEALING ARRANGEMENT THROUGH SEALING
DEAD ENDEDLIQUID PUMPEDFOREIGN LIQUID
GREASEBLEED OFF
MECHANICAL SEAL API CODEOMAKEΔ/
FLUSH WITH
MANUFACTURER MAT'L CODEΔ/
MODELΔ/
API CODE MAT'LΔ/ 3RD LETTER4TH LETTER5TH LETTER
PIPING FOR PRIMARY SEAL API FIG. D-2 PLANOPIPING FOR THROTTLE BUSHING OROAUXILIARY SEAL API FIG. D-3 PLANCOOLING WATER PIPING, API FIG. D-4 PLANOCYCLONE SEPARATOR YESO NOOFLOW ORIFICE IN SEAL FLUSH SUPPLY LINE YESO NOOSEAL LEAKAGE PIPING WITH ORIFICE YESO NOOBUFFER LIQUID SYSTEM YESO NOOMETHANOL DRIP SYSTEM YESO NOOREQUIRED: PRESSUREΔ/ PSIG; FLOW USGPM
CARTRIDGE DESIGN YESO NOO
WIDTH. IMPELLER DISCH. IN
UNDER / OVER FILING / V-CUT YES / NO
WEARING RINGS:IMPELLERCASECLEARANCE ININBOARD
OUTBOARD IN
1st STAGE IMPELLER INLET GEOMETRY
Dp =
Dp
Dsl
Dh1 Dh2
d
α h
α p
Dsl =Dh1 =Dh2 =d =α p =α h =
ININ (IF APPLICABLE)INININDEGREESDEGREES
YESYES
NO
NO
GE‐103004
A
09-17-2011
NM
09-17-2011
09-17-2011
09-1
7-2
CENTRIFUGAL PUMP
SAUDI ARABIA
2 of 4 00
NOTE:
RADIAL
CONSTRUCTION DATA (CONT'D) CONSTRUCTION DATA (CONT'D)
DESCRIP
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NJO
OPR
NS
EN
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PMT
CERT
E
CENTRIFUGAL PUMP DATA SHEET FOR HORIZONTAL PUMPS AND VERTICAL IN-LINE PUMPS
BY MANUFACTURER OF PUMPS OR PUMPS PER API 610
BY MANUFACTURER OF PUMPS PER ASME B 73.1 OR B 73.2O INDICATES INFORMATION TO BE COMPLETED BY PURCHASER;
BEARING TYPE
BEARINGS AND LUBRICATION
Δ/
COUPLING
SLEEVEANTI-FRICTIONTILTING PAD
GREASERING-OIL CONSTANT LEVELLUBRICATOR, MAKEOIL BATH WITH EXT'L CIRCULATIONFORCED FEEDOIL MISTLUBE OIL PIPING TO ANDFROM BEARINGSLUBE OIL PIPING UP TO L.O. SYSTEMTERMINATION WITH FLANGEDCONNECTIONS AT RADIAL COUPLINGPLANE
RADIAL THRUST
SIGHT FLOW INDICATOR IN EACHRETURN BRANCH MAKETHRUST BEARING LOADS:MAX. ALLOWABLE AXIAL FORCE:DESIGN AXIAL FORCE:
THRUST
YESYES
NONO
YES NO
NN
LUBRICANTSBEARING LUBRICANTOIL O GREASE O
Δ/ MAKE MODEL SIZESUPPLIED BY:
DIAPHRAGMO
TYPEDISC PACKO
RIGID ADJUSTABLEOCLOSE COUPLEDOELASTOMERICOHYDRAULIC FIT KEYED
SPACER: YES,O NOOINCOUPLING GUARD O PARTIALLY ENCLOSED COMPLETELY ENCLOSEDPUMP SHAFT END CYLINDRICAL TAPEREDMOUNT COUPLING HALF: PUMP YES NO
DRIVER HALF YES NO. IF SHIPPED TO DRIVER SUPPLIERPILOT BORED COMPLETELY MACHINED
MODELBASE PLATEO
BASE PLATE
O OIL FIELD SKIDSUPPLIED BYO PUMP VENDORTO ACCOMMODATE: DRIVER GEAR PUMP OL.O. AND/OR S.O. SYSTEM MOUNTED O ON BASE O OFF BASEDESIGNED FOR INSTALLATION ON:O CONCRETE FOUNDATION O STEEL PLATFORMDRILLED FOR DRIVER O YES O NO GEAR O YES O NOHORIZONTAL ALIGNMENT JACKSCREWS O YES O NO
O O O
LUBRICATION METHOD
0008
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DATE:
PROJECTENGINEER
CONSTRUCTIONAGENCY
SR
3 f 4 00
OPERATION
CERTIFIED
REV.NO.SHT.NO.DRAWING NO.DATA SHEET FOR
DATE
REV.
NO
.
ENGINEERDISCIPLINE
DATE:
DATE:
DCO
DATE:
DATE:
MAX. OILOUTL. TP.
HEATREMOVAL
SUPPLYPRESSURE
FLOW ORCAPACITY
OFBTU/MINPSIGGPM/USGALINB. BRG.OUTB. BRG.THRUST BRG.
TOTALLUBE OIL SYSTEM SUPPLIED BY: PUMP VENDORO
OTHEROIN ACCORDANCE WITH DATA SHEET FORM 8004-ENG
YES, DRAWING NO.O NOO
COOLINGBEARING COOLINGNON-CIRCULATING SYSTEM BY:
SHAFT MOUNTED FANCOILS IN BEARING HOUSING
JACKETED BEARING HOUSING
EXTERNAL CIRCULATING SYSTEMOIL COOLING BY:
LIQ. PUMPED FOREIGN LIQ. AIR NONEYES NOYES NO
STUFFING BOX COOLINGPEDESTAL COOLINGCOOLING PIPING FOR
BEARINGS STUF. BOX PEDESTALS SEAL COOLERIN ACCORDANCE WITH API-610. FIG. D-4.
SEALCOOLER
INLET PRESS.TEMP. INLETTEMP. OUTLETCOOLING MEDIUM
TOTAL FLOW USGPM
PEDES-TAL
STUFBOX
BRGHSG
PSIGOFOF
VENDOR TO COMPLETE FOLLOWING MAT'L LISTING (Note 2)Δ/ 1. CASING
2. IMPELLER(S)3. CASE WEAR RINGS4. IMPELLER WEAR RINGS
A743CF8MASTMA743CF8MASTM
ASTMASTM
5. SHAFT A276 XM19ASTM6. SHAFT SLEEVES SS316ASTM7. THROAT BUSHINGS A276 316ASTM8. INTERSTAGE SLEEVES N/AASTM9. INTERSTAGE BUSHINGS N/AASTM10. LANTERN RING (PACKED PUMPS) N/AASTM11. GLAND / MECH. SEAL FLANGE ASTM12. BEARING BRACKETS A216 WCBASTM13.1 NON-WETTED STUDS / NUTS A193-B7/A194-GR 2HASTM13.2 WETTED FASTENERS ASTM14. PIPING: PIPE / FITTINGS ASTM15. BASE PLATE A36ASTM16. MECH. SEAL SPRINGS ASTM17. MECH. SEAL OTHER METAL PARTS ASTM18. ASTM19. ASTM
NOISE SPECIFICATION
MAXIMUM ALLOWABLE SOUND LEVELO
BY PURCHASER AT 3 FT. DISTANCE 85MANUFACTURER GUARANTEED MAXIMUMPUMPDRIVEROTHERCOMPLETE TRAIN 85
dBA
dBAdBAdBAdBA
COOLANT DATA
MATERIALS OF CONSTRUCTION
A
GE‐103004
09-17-2011
NM
09-17-2011
09-17-2011
09-1
7-2
CENTRIFUGAL PUMP
SAUDI ARABIA Job No :
3 of 4 00JUBAIL
NOTE:
UTILITIES INSPECTION AND TESTS
DESCRIP
TIO
NO
PRN
SEN
GG
PMT
CERT
TE
CENTRIFUGAL PUMP DATA SHEET FOR HORIZONTAL PUMPS AND VERTICAL IN-LINE PUMPS
BY MANUFACTURER OF PUMPS OR PUMPS PER API 610
DRAWINGS AND OTHER DATA
ELECTRIC POWERO
OO
OO
O
BY MANUFACTURER OF PUMPS PER ASME B 73.1 OR B 73.2O INDICATES INFORMATION TO BE COMPLETED BY PURCHASER;
AVAILABLE
VOLTS
3/60480AC1/60120AC
ACDC
PHASEHZ
MAIN ELECTRIC DRIVERCONTROLS AND PROTECTION
AIRO AVAILABLEPSIG
CONTROLS AND PROTECTION
INLETOF
AVAILPSIG
WATER
REQ'DOF
OUTLETOFAVAIL COOLING
WELL WATEROONCE THROUGH SYSTEMO
TREATED WATERO SEA WATEROCLOSED LOOP SYSTEMO
INSTRUMENTATION & CONTROLS
CASINGTHERMOWELL
THRUSTBEARINGS
RADIALBEARINGS
OO
OO
OO
OF
TEMPERATUREMONITORING
YESPROVISIONS ONLY
ALARM SETTING
VENDOR'S STANDARD SHOP TESTOAS FOLLOWSHYDROSTATIC TEST N
ON
E
WATERO KEROSENEO
CER
T'D
OB
SER
'D
WIT
N'D
RUNNING TESTPERFORMANCE TESTMEASURE ΔP ACROSS STUFFING BOXNPSH TESTDISMANTLINGRADIOGRAPHIC INSPECTION IMPELLERDYE PENETRANT EXAMINATION IMPELLERDYNAMIC BALANCE IMPELLER(S)DYNAMIC BALANCE ROTORDYNAMIC BALANCE COUPLINGVIBRATION, MEASUREMENTSTESTS TO BE CARRIED WITH:
O
O
OO
O
OO
O
OO
OO
O
O
O
OO
O
OO
O
OO
OO
O
O
O
OO
O
OO
O
OO
OO
O
O
O
OO
O
OO
O
ACTUAL DRIVERO MANUFACTURER'S DRIVERO
AT O RATED SPEED O DERATED SPEED: RPM
MANUFACTURER'S DRAWING OR DOCUMENT NO.REQUIRED
NOYESDIMENSIONAL DRAWING OFCOMPLETELY ASSEMBLED UNIT OO
O
0008
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O-2
011
grades for the specified service.
for application.
1- Vendor shall confirm the material selection and ASTM
2- Vendor standard pump may be acceptable if better suits
3- Provision shall be provided for mechanical seal installation in future.4- Liquid may contain traces of Cr, Pb, Cd etc.
DATE:
PROJECTENGINEER
CONSTRUCTIONAGENCY
SR
OPERATIONS
CERTIFIED
REV.NO.SHT.NO.DRAWING NO.DATA SHEET FOR
DAT
REV.
NO
.
ENGINEERDISCIPLINE
DATE:
DATE:
DCO
DATE:
DATE:
OF
VIBRATION / DISPLACEMENT MONITORING
BRG. HSGSEISMIC
THRUST BRG.PROXIMITY
RADIAL BRG'SPROXIMITY
ALARM SETTINGSHUTDOWN SETTING
POSITIONTYPE
YESPROVISIONS ONLY
OO
OO
OO
Δ
//
/ALARM / SHUTDOWNSETTING:
MILS P-PMILS P-P
IN / SEC RMS
SEISMICO OO
PNEUMATICELECTRICAL
PROXIMITYO
SHAFT SEAL LEAKAGE CONTROL: YESELECTRICALO PNEUMATICO
PRES. SWITCH MAKE MODELΔ PRESSURE SETTING *SHUTDOWN* PSIG
LEVEL SWITCH MAKE MODELΔ TIME DELAY SETTING CONTR.ORIFICE IN
MASSES
Δ PUMP LBSPUMP ROTATING ASSEMBLY LBSCASING (UPPER HALF) LBSBASEPLATE LBSCOUPLING LBS
DRIVER LBS
DRIVER ROTATING ASSEMBLY LBS
TOTAL MASS LBS
COMPLETELY ASSEMBLED UNIT OOOPER. & MAINT. INSTRUCTIONS OOCROSS SECT. DRW. WITH PART NO'S. OOMECHANICAL SEAL DRAWING OOBILLS OF MATERIALS OOCOMPLETED PUMP DATA SHEET OOAUXILIARY PIPING DWG. OOCERTIFIED TEST CURVE & DATA OORECOMMENDED SPARES LIST OOINSTR. WIRING DIAGRAM OOSPEED TORQUE CURVE OOCOLD ALIGNMENT CURVE OODATA L. & T. VIBR. ANALYSIS OO
MISCELLANEOUS
BUYER'S PAINT SPECIFICATION:
PAINTING
O
VENDOR'S STANDARD:O
SPECIFICATION
API 610
PUMPS TO BE IN ACCORDANCE WITH:
O
ASME B 73.1O ASME B 73.2O
O
ONOTES:
NOO
GE‐103004
A
MANUFACTURER'S STANDARD (Note 2)
09-17-2011
NM
09-17-2011
09-17-2011
09-1
7-
OTHER LIQUID TRANSFER PUMPS TAG# P-104A/B
CENTRIFUGAL PUMP
SAUDI ARABIA
4 of 4 00GE‐103004
