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

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



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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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



RFCC-A-47-PR-DS-P522

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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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SERVICE : NAPHTHA PUMP

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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




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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


BEARINGS AND LUBRICATION

4 23-Apr-13 NK/JH MF/MJ IRJ/AF

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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




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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


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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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




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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


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

47-p-522 naphta pump rev 4

Documents

operating pressure

efficiency2 page

record4 page

discharge pressure kgcmg

suction pressure kgcmg

motor item

vendor datasheet4 page

pump item