47-P-522 Naphta Pump Rev 4
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Transcript of 47-P-522 Naphta Pump Rev 4
-
Rev. No. :
Cilacap Resid Fluid CatalyticCracking (RFCC) Project
PT. PERTAMINA (Persero)
Doc. No. :RFCC-A-47-PR-DS-P522
4
Naphtha Pump Process Data Sheet Page No. : 2/7
REVISION HISTORICAL SHEET
Rev. Page /Paragraph Item Description of change
2 Page 4 Performance Add Rated Power and Efficiency
2 Page 7 Note Add Note 2, 3 & 4
1 - General Change Process Datasheet format
2 Page 4 Oper. Condition & PerformanceChange Suction Press. Rated, Differential Press., NPSHA, Hydraulic Power, Est. Shutoff Press.
4 Page 4 Performance Update Shutoff Pressure, Rated Power and Efficiency as per Vendor datasheet
4 Page 4 Size and Utility Data Update Phase of Electricity for Drivers
3 - - Issued for Record
4 Page 4 Operating ConditionUpdate Max & Rated Suction Pressure and Discharge Pressure due to update Pump Centerline from Vendor drawing
Update Nozzle Condition and Pressure Casing Connections
4 Page 4 Performance Add Impeler Diameter, Max Head and NPSHR as per Vendor datasheet
4 Page 5 Material Update material class as per Vendor datasheet
CONSORTIUM ADHI - GS E&C
4 Page 5 Construction
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CILACAP RESID FLUID CATALYTIC CRACKING (RFCC) PROJECT Rev. Prep'd Check'd Appr'd DatePERTAMINA RU-IV CILACAP, CENTRAL JAVA, INDONESIA A MF MF/MJ IRJ/AF 23-Dec-11PT. PERTAMINA (PERSERO) 0 NK MF/MJ IRJ/AF 10-Jan-12RFCC-A-47-PR-DS-P522 1 NK MF/MJ IRJ/AF 23-Feb-1215/C00000/2011-S2 2 NK MF/MJ IRJ/AF 22-May-122F1102 3 NK MF/MJ IRJ/AF 26-Jun-12
4 NK/JH MF/MJ IRJ/AF 23-Apr-13
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REFERENCE LIST
47-P-522 NAPHTHA PUMP
Description ITB SN CN EPC Rev. 4
PROJECT TITLE
Cilacap Resid Fluid CatalyticCracking (RFCC) Project
PT. PERTAMINA (Persero)
JOB NO.PAGE 3 OF 7
DOC. NO.CLIENT JOB NO.
LOCATIONOWNER
Flow Normal (m/h) - - - -
Flow Rated (m/h) 300 - - 300
Relative Density (SG) - -
Source:Operating Pressure:
0.005Destination:
Operating Pressure:6
(Min) : 0.77(Normal): 0.724
(Min) : 0.77(Normal): 0.724
Pumping Temperature (C) - -
Basis:Pressure (kg/cmG) - - -
(Min) : 18(Normal): 38
(Min) : 18(Normal): 38
Viscosity (cP) (Normal) :0.41 - - 0.41
Vapor Pressure (kg/cm) (Normal)0.51 - - 0.51
Suction Pressure (kg/cmg) -0.02 - - -0.07
Discharge Pressure (kg/cmg) 9.16 9.11
Differential Pressure (kg/cm) 9.18 - - 9.18
Differential Head (m) 126.98 - - 126.98
NPSHA (m) 6.20 - - 6.20
Plot Plan - - - General Plot Plant Rev. 2A
Suction Reservoir - - - Naphtha Tank
Outlet Destination - - - Gasoline from RFCC Unit 105(ISBL -OSBL Battery Limit)
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Rev. No. :
Page No. :
Item No. : 47-P-522Unit : TANKAGE UNITNo. Of Units : 1 (Operation) Driven by : Motor
Service : NAPHTHA PUMP
REV
APPLICABLE TO: PROPOSALS PURCHASE AS BUILT 1
FOR UNIT 2
SITE SERVICE 3
NO. REQ PUMP SIZE TYPE NO. STAGES 4MANUFACTURER MODEL SERIAL NO. 5
NOTES: INFORMATION BELOW TO BE COMPLETED: BY PURCHASER BY MANUFACTURER BY MANUFACTURER OR PURCHASER 6
7
PUMPS TO OPERATE IN (PARALLEL) NO. MOTOR DRIVEN NO. TURBINE DRIVEN 8(SERIES) WITH PUMP ITEM NO. PUMP ITEM NO. 9GEAR ITEM NO. MOTOR ITEM NO. TURBINE ITEM NO. 10
GEAR PROVIDED BY MOTOR PROVIDED BY TURBINE PROVIDED BY 11
GEAR MOUNTED BY MOTOR MOUNTED BY TURBINE MOUNTED BY 12
GEAR DATA SHT. NO. MOTOR DATA SHT. NO. TURBINE DATA SHT. NO. 13
14
CAPACITY, NORMAL m/h RATED m/h WATER SOURCE 15
OTHER m/h CHLORIDE CONCENTRATION (PPM) 164 SUCT PRESS MAX./RATED / kg/cm[g] INSTRUMENT AIR: MAX/MIN PRESS / 17
4 DISCHARGE PRESSURE kg/cm[g] 18
DIFFERENTIAL PRESSURE kg/cm TYPE OR NAME OF LIQUID 19DIFF. HEAD m NPSHA m PUMPING TEMPERATURE 20
PROCESS VARIATIONS NORMAL C MAX. C MIN. 21
STARTING CONDITIONS VAPOR PRESSURE kg/cm [a] @ C 22SERVICE: CONT. INTERMITTENT (STARTS/DAY) RELATIVE DENSITY (SPECIFIC GRAVITY): 23
PARALLEL OPERATION REQ'D NORMAL MAX MIN 24SPECIFIC HEAT kcal/(kg.C) 25
LOCATION: VISCOSITY cP @ C 26
INDOOR HEATED UNDER ROOF MAX. VISCOSITY cP 27
OUTDOOR UNHEATED PARTIAL SIDES CORROSIVE/EROSIVE AGENT 28
GRADE MEZZANINE CHLORIDE CONCENTRATION (PPM) 29ELECTRIC AREA CLASSIFICATION H2S CONCENTRATION (PPM) 30
CL GR DIV LIQUID HAZARDOUS FLAMMABLE 31WINTERIZATION REQ'D TROPICALIZATION REQ'D. OTHER 32
HYDROGEN PARTIAL PRESSURE
SITE DATA See "Basic Engineering Design Data" 33ALTITUDE BAROMETER PROPOSAL CURVE NO. RPM 34
RANGE OF AMBIENT TEMPS: MIN/MAX. / IMPELLER DIA. RATED MAX. MIN. mm 35
4 RELATIVE HUMIDITY: MIN / MAX / % HYDRAULIC POWER kW 36
4 RATED POWER kW EFFICIENCY %
UNUSUAL CONDITIONS: DUST FUMES MINIMUM CONTINUOUS FLOW: 37
OTHER THERMAL m/h STABLE m/h 38
UTILITY CONDITIONS: See "Basic Engineering Design Data" PREFERRED OPERATING REGION TO m/h 39STEAM: ALLOWABLE OPERATING REGION TO m/h 40
MIN MAX HEAD @ RATED IMPELLER m 41
MAX MAX POWER @ RATED IMPELLER kW 42
4 ELECTRICITY HEATING CONTROL SHUTDOWN NPSHR AT RATED CAPACITY m 43
VOLTAGE SUCTION SPECIFIC SPEED 44
HERTZ MAX. SOUND PRESS. LEVEL REQ'D (dBA) 454 PHASE EST MAX SOUND PRESS. LEVEL (dBA) 46
COOLING WATER: REMARKS: 47
TEMP. INLET C MAX. RETURN C 48
PRESS. NORM kg/cm[g] DESIGN kg/cm[g] 49MIN RETURN MAX ALLOW DP kg/cm 50
4 FOULING FACTOR SHUTOFF PRESSURE kg/cm[g] 51
107.0 74.29
Cilacap Resid Fluid CatalyticCracking (RFCC) Project
PT. PERTAMINA (Persero)
RFCC-A-47-PR-DS-P522
4
4 of 7Rev DATE PRED REVD APVDA 23-Dec-11 MF MF/MJ IRJ/AF0 10-Jan-12 NK MF/MJ IRJ/AF1 23-Feb-12 NK MF/MJ IRJ/AF2 22-May-12 NK MF/MJ IRJ/AF3 26-Jun-12 NK MF/MJ IRJ/AF4 23-Apr-13 NK/JH MF/MJ IRJ/AF
1
NAPHTHA PUMP
GENERAL
147-P-522
OPERATING CONDITIONS (5.1.3) SITE AND UTILITY DATA (CONT'D)300
9.18 Naphta126.98 6.20
38 18
1.16 -0.07
9.11 LIQUID
SITE AND UTILITY DATA
0.41 38
None
0.510 38
0.724 0.770
PERFORMANCE
1 IIA / IIB T3
18 37 304 381 291100 79.90
See "Basic Engineering Design Data"
DRIVERS HEATING
DRIVERS 3.113300 220
144.3
33 463.2 6.5
1
50 50 853 1
12.27
CONSORTIUM ADHI - GSEC
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ITEM No. :
SERVICE : NAPHTHA PUMP
REV
1
APPLICABLE STANDARD: SHAFT DIAMETER BETWEEN BEARINGS mm 2
API 610 10TH EDITION SPAN BETWEEN BEARING CENTERS mm 3
OTHER (SEE REMARKS) SPAN BETWEEN BEARING & IMPELLER mm 4PUMP TYPE: REMARKS 5
OH2 BB1 VS1 VS6 6
OH3 BB2 VS2 VS7 7
OH4 BB3 VS3 OTHER COUPLINGS: DRIVER - PUMP 8
OH5 BB4 VS4 MAKE 9
OH6 BB5 VS5 MODEL 10
NOZZLE CONDITIONS: RATING 11
SIZE (IN) FLANGE FAC'G POSITION LUBRICATION 12CLASS LIMITED END FLOAT REQUIRED 13
4 SUCTION SPACER LENGTH mm 14
4 DISCHARGE SERVICE FACTOR 15
BALANCE DRUM DRIVER HALF COUPLING MOUNTED BY: 16
PRESSURE CASING CONNECTIONS: PUMP MFR. DRIVER MFR. PURCHASER 17NO. SIZE (NPS) TYPE COUPLING PER API 671 18
4 DRAIN BASEPLATES: 19
4 VENT (IF NOT SELF VENT) API BASEPLATE NUMBER (APPENDIX M) 20PRESSURE GAUGE NON-GROUT CONSTRUCTION: 21
TEMP GAUGE REMARKS: 22
WARM-UP 23
BALANCE / LEAK-OFF 24
CYLINDRICAL THREADS REQUIRED 254 CASING MOUNTING: ( SEE SEPARATE SHEET FOR VERTICALS) APPENDIX H CLASS 26
CENTERLINE NEAR CENTERLINE MIN DESIGN METAL TEMP C 27
FOOT SEPARATE MOUNTING PLATE BARREL/CASE IMPELLER 28
IN-LINE CASE/IMPELLER WEAR RINGS 29
CASING SPLIT: SHAFT 30
AXIAL RADIAL DIFFUSERS 31
CASING TYPE: COUPLING SPACER/HUBS 32
SINGLE VOLUTE MULTIPLE VOLUTE DIFFUSER COUPLING DIAPHRAGMS (DISKS) 33OVERHUNG BETWEEN BEARINGS BARREL REMARKS: 34
CASE PRESSURE RATING: 35
MAX ALLOWABLE WORKING PRESSURE kg/cm[g] 36
@ 0 37
HYDROTEST PRESSURE kg/cm[g] BEARING (TYPE/NUMBER): 38SUCT'N PRESS. REGIONS MUST BE DESIGNED FOR MAWP RADIAL / 39
ROTATION: (VIEWED FROM COUPLING END) THRUST / 40CW CCW REVIEW AND APPROVE THRUST BEARING SIZE 41
IMPELLERS INDIVIDUALLY SECURED LUBRICATION: 42
REMARKS: GREASE FLOOD RING OIL 43
FLINGER PURGE OIL MIST PURE OIL MIST 44
BOLT OH3 PUMP TO PAD/FOUNDATION CONSTANT LEVEL OILER PREFERENCE (SEE REMARKS) 45SHAFT: PRESSURE LUBE SYS API-610 API-614 46
SHAFT DIAMETER AT COUPLING mm OIL VISC. ISO GRADE 47
REMARKS: SUCTION TYPE 48
IMPELLER TYPE 49
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47-P-522 Rev DATE PRED REVD APVD
Cilacap Resid Fluid CatalyticCracking (RFCC) Project
PT. PERTAMINA (Persero)
RFCC-A-47-PR-DS-P522
4
5 of 7
A 23-Dec-11 MF MF/MJ IRJ/AF0 10-Jan-12 NK MF/MJ IRJ/AF1 23-Feb-12 NK MF/MJ IRJ/AF
2 22-May-12 NK MF/MJ IRJ/AF3 26-Jun-12 NK MF/MJ IRJ/AF
CONSTRUCTION CONSTRUCTION (CONT)
8" 300# RF Top
1 3/4" Provide with Valve
6" 300# RF Top
MATERIAL
S-618
CONSORTIUM ADHI - GSEC
BEARINGS AND LUBRICATION
4 23-Apr-13 NK/JH MF/MJ IRJ/AF
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REV
1
OIL HEATER REQ'D ELECTRIC STEAM VAPOR PRESSURE kg/cm [a] @ C 2OIL PRESS TO BE GREATER THAN COOLANT PRESS HAZARDOUS FLAMMABLE OTHER 3
REMARKS FLOW RATE MAX/MIN / m/h 4
PRESSURE REQUIRED MAX/MIN / kg/cm[g] 5TEMPERATURE REQUIRED MAX/MIN / 0 6
QUENCH FLUID: 7SEAL DATA: NAME OF FLUID 8
SEE ATTACHED API-682 DATA SHEET FLOW RATE m/h 9
NON-API 682 SEAL SEAL FLUSH PIPING: 10
APPENDIX H SEAL CODE SEAL FLUSH PIPING PLAN 11
SEAL MANUFACTURER TUBING CARBON STEEL 12
SIZE AND TYPE / PIPE STAINLESS STEEL 13
MANUFACTURER CODE AUXILIARY FLUSH PLAN 14
SEAL CHAMBER DATA: TUBING CARBON STEEL 15
TEMPERATURE PIPE STAINLESS STEEL 16
PRESSURE kg/cm[g] PIPING ASSEMBLY: 17FLOW m/h THREADED UNIONS SOCKET WELDED 18
SEAL CHAMBER SIZE (TABLE 2.3) FLANGED TUBE TYPE FITTINGS 19TOTAL LENGTH mm CLEAR LENGTH mm LOW PRESSURE SWITCH (PLAN 52/53) TYPE 20
SEAL CONSTRUCTION: PRESSURE GAUGE (PLAN 52/53) 21SLEEVE MATERIAL LOW LEVEL SWITCH (PLAN 52/53) TYPE 22GLAND MATERIAL LEVEL GAUGE (PLAN 52/53) 23AUX SEAL DEVICE TEMP INDICATOR (PLANS 21, 22, 23, 32, 41) 24JACKET REQUIRED HEAT EXCHANGER (PLAN 52/53) 25
GLAND TAPS: REMARKS 26
FLUSH (F) DRAIN (D) BUFFER (B) 27QUENCH (Q) COOLING (C) LUBRICATION (G) 28HEATING (H) LEAKAGE PUMPED FLUID (P) VIBRATION: 29BAL'NCE FLUID (E) EXTERNAL FLUID INJECTION (X) NONCONTACTING (API 670) TRANSDUCER 30
SEAL FLUIDS REQUIREM'T AND AVAILABLE FLUSH LIQUID: PROVISION FOR MOUNTING ONLY 31NOTE: IF FLUSH LIQUID IS PUMPAGE LIQUID (AS IN FLUSH PIPING FLAT SURFACE REQ'D 32PLANS 11 TO 41), FOLLOWING FLUSH LIQUID DATA IS NOT REQ'D. SEE ATTACHED API 670 DATA SHEET 33
SUPPLY TEMPERATURE MAX/MIN / C MONITORS AND CABLES 34
RELATIVE DENSITY (SPECIFIC GRAVITY) @ C REMARKS 35
NAME OF FLUID 36
SPECIFIC HEAT kcal/(kg.C) COOLING WATER PIPING PLAN 37VAPOR PRESSURE kg/cm [a] @ C COOLING WATER REQUIREMENTS 38HAZARDOUS FLAMMABLE OTHER SEAL JACKET/BRG HSG m/h @ kg/cm[g] 39FLOW RATE MAX/MIN / m/h SEAL HEAT EXCHANGER m/h @ kg/cm[g] 40PRESSURE REQUIRED MAX/MIN / kg/cm[g] QUENCH m/h @ kg/cm[g] 41TEMPERATURE REQUIRED MAX/MIN / TOTAL COOLING WATER m/h 42
BUFFER FLUID: STEAM PIPING: TUBING PIPE 43
SUPPLY TEMPERATURE MAX/MIN / C REMARKS Sight Flow Indicators shall be provided 44RELATIVE DENSITY (SPECIFIC GRAVITY) @ C 45NAME OF FLUID 46
ADDITIONAL REMARKS: 47
48
49
50
51
MF MF/MJ IRJ/AF
Cilacap Resid Fluid CatalyticCracking (RFCC) Project
PT. PERTAMINA (Persero)
RFCC-A-47-PR-DS-P522
4
6 of 7
ITEM No.: 47-P-522Rev DATE PRED
SERVICE : NAPHTHA PUMP0 10-Jan-12 NK MF/MJ IRJ/AF1 23-Feb-12 NK MF/MJ IRJ/AF
BEARINGS AND LUBRICATION (CONT) MECHANICAL SEAL OR PACKING (CONT)
MECHANICAL SEAL OR PACKING
API Plan 11
CONSORTIUM ADHI - GSEC
INSTRUMENTATION
STEAM AND COOLING WATER PIPING
4 MF/MJ IRJ/AF23-Apr-13 NK/JH3 26-Jun-12 NK MF/MJ IRJ/AF2 22-May-12 NK MF/MJ IRJ/AF
REVD APVDA 23-Dec-11
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Page No. :
REV
NOTES:1. For utility and site conditions, please refer to "Basic Engineering Design Data" (RFCC-C-000-PR-SP-001)
4 2. Hydraulic data refer to Hydraulic Calculation Report unit 47 Rev. 7 (Doc. No.: RFCC-A-47-PR-CS-001)3. NPSHR at least 1 (one) meter below NPSHA.
4 4. Basis of Calculation (BOC), Pump routing sketch (Source and Destination), Calculation Sheet, Line Pressure Drop include Pressureprofile calculation and Process Design Information describe calculation summary (comparation) between ITB vs EPC can be seenin Hydraulic Calculation Reports Unit 47 Rev. 7 (Doc. No.: RFCC-A-47-PR-CS-001).
ITEM No. : 47-P-522REV DATE PRED
Cilacap Resid Fluid CatalyticCracking (RFCC) Project
PT. PERTAMINA (Persero)
RFCC-A-47-PR-DS-P522
4
Page 7 of 7REVD APVD
A 23-Dec-11 MF MF/MJ IRJ/AF
SERVICE : NAPHTHA PUMP0 10-Jan-12 NK IRJ/AF1 23-Feb-12 NK MF/MJ IRJ/AF
MF/MJ
CONSORTIUM ADHI - GSEC
2 22-May-12 NK MF/MJ IRJ/AF3 26-Jun-12 NK MF/MJ IRJ/AF4 23-Apr-13 NK/JH MF/MJ IRJ/AF