Project No. 19911 Detail Engineering & Procurement Support ...

Project No. 19911

Detail Engineering & Procurement Support Services for Feruka – Harare Pipeline Series Operation

Comments Resolution Sheet (CRS)

of 1

Doc. No. 19911-ME-DAT-

WIL-0001 Rev.

A Vendor

Doc. No. Rev. A Trans Ref.: 19911-PZL-PIL-TM-0081

Trans. Date: 31-03-2021

Doc. Title: DATA SHEET FOR MAINLINE PUMPS (API-610)-WILTON PUMP STATION

Status Code : 1 Code 1-Approved no comments, Code 2-Approved with comments, Code 3-Revise as noted, Code 4- For information

S/N Section /Page Ref. COMPANY Comments CONTRACTOR Reply Status /

Remarks

1. - No Comments Noted, document has been issued for next revision (Rev 0).

2. Seal Support System (Plan 65) shall be mounted on the pump base plate.

Page 6 of 12

3.

Dual (Arrangement 2) Mechanical Seal is proposed in line with Specification requirement. Same is for further check/confirmation from pump/seal vendor during bidding.

Page 9 of 12

4.

5.

6.

7.

8.

DATA SHEET FOR MAINLINE PUMPS (API-610)-WILTON

PUMP STATION

0

A

REV.

Revision : 0

Date: 27-04-2021

Page: 1 of 12

Project No. 19911

Detail Engineering & Procurement Support Services

for Feruka – Harare Pipeline Series Operation

© Copyright Penspen 2021. All rights reserved

All data and information contained herein confidential and the property of Penspen.  The data and information contained herein may

not be reproduced, published or distributed to, or for, any third parties without the express prior written consent of Penspen.

Issued for Construction27-04-2021 UJ KA AW

DESCRIPTION

30-03-2021 UJ KA AW Issued for Review

DATE ORIGINATOR REVIEWED APPROVED APPROVED

ORGINATOR Project No: 19911

THIS DOCUMENT IS INTENDED FOR USE BY ADNOC AND ITS NOMINATED CONSULTANTS, CONTRACTORS, MANUFACTURERS AND SUPPLIERS.

COMPANY: Petrozim Line (PVT) Limited

ORIGINATOR: Penspen International Limited

Document No. : 19911-ME-DAT-WIL-0001

DATA SHEET FOR MAINLINE PUMPS (API-610)-WILTON PUMP STATIONDocument No. : 19911-ME-DAT-WIL-0001 Rev : 0

Project No. : 19911 Page : 2 of 12

The table below is a brief summary of the most recent revisions to this document. Details of all revisions are held on

document by the issuing department.

Sr. No. Rev. No. Issue No. Date of issue Description of revision

2 0 2 27-04-2021 ISSUED FOR CONSTRUCTION

1 A 1 30-03-2021 ISSUED FOR REVIEW

DATA SHEET FOR MAINLINE PUMPS (API-610)-WILTON PUMP STATION

Document No. : 19911-ME-DAT-WIL-0001 Rev : 0

Project No. : 19911 Page : 3 OF 12

INDEX

SIGNATURE

COVER

8

1

2

3

4

5

6

7 A

TAG NO. REVISION

11 GENERAL NOTES

REMARKPAGE

X

HISTORY REVISION

A

9 MECHANICAL SEAL DATASHEET

PUMP DATA SHEET

PUMP DATA SHEET

PUMP DATA SHEET

PUMP DATA SHEET

PUMP DATA SHEET

10 MECHANICAL SEAL DATASHEET

12 GENERAL NOTES




1 APPLICABLE TO: APPLICABLE NTL/INTNTL STANDARD: Rev

2 FOR ITEM NO.

3 SITE SERVICE

4 NO. REQ PUMP SIZE TYPE No. Stages

5 MANUFACTURER MODEL SERIAL NO.

6

7 SERVICE :

8 LIQUID TYPE OR NAME : • IF INTERMITTENT NO. OF STARTS :

9 VAPOR PRESSURE : PUMPS OPERATE IN:

10 CORROSION DUE TO : (6.12.1.9)

11 SPECIFIC HEAT : EROSION DUE TO : (6.12.1.9)

12 VISCOSITY : H2S CONCENTRATION (ppm) : (6.12.1.12)

13 CHLORIDE CONCENTRATION (ppm) :

14 PARTICULATE SIZE (DIA IN MICRONS)

15 NPSHa Datum: PARTICULATE CONCENTRATION (PPM)

16 PUMPING TEMPERATURE : REMARKS:

17 FLOW :

18 DISCHARGE PRESSURE : (6.3.2)

19 SUCTION PRESSURE :

20

21

22

23

24

25 LOCATION: COOLING WATER :

26

27 MOUNTED AT : l TEMP o C MAX

28 ELECTRIC AREA CLASSIFICATION: 6.1.22 ZONE PRESS. barg MIN

29 GROUP TEMP CLASS SOURCE

30 SITE DATA : COOLING WATER CHLORIDE CONCENTRATION: ppm

31 ELEVATION (MSL) : m BAROMETER : mmHg INSTRUMENT AIR : MAX barg MIN barg

32 RANGE OF AMBIENT TEMPS:MIN / MAX / o C STEAM

33 RELATIVE HUMIDITY: MIN / MAX / %

34 UNUSUAL CONDITIONS: TEMP o C Max

35 Min

36 UTILITY CONDITIONS : PRESS. barg Max

37 ELECTRICITY : Min

38 VOLTAGE

39 PHASE

40 HERTZ

41

42 PROPOSAL CURVE NO. RPM Driver Type

43 As Tested Curve No. GEAR

44 IMPELLER DIA.: RATED MAX. MIN. mm VARIABLE SPEED REQUIRED

45 RATED POWER kW EFFICIENCY (%) SOURCE OF VARIABLE SPEED

46 RATED CURVE BEP FLOW (at rated impeller dia) m3/hr. OTHER

47 MIN FLOW : THERMAL m3/hr. STABLE m3/hr. MANUFACTURER

48 PREFERRED OPERATING REGION (6.1.11) to m3/hr. NAMEPLATE POWER kW

49 ALLOWABLE OPERATING REGION to m3/hr. Nominal RPM

50 MAX HEAD @ RATED IMPELLER m RATED LOAD RPM

51 MAX POWER @ RATED IMPELLER (6.8.9) kW FRAME OR MODEL

52 NPSH3 AT RATED FLOW : m ORIENTATION

53 CL PUMP TO U/S BASEPLATE m LUBE

54 NPSH MARGIN AT RATED FLOW : m BEARING TYPE:

55 SPECIFIC SPEED (6.1.9) RADIAL

56 SUCTION SPECIFIC SPEED LIMIT 11000 US Units THRUST

57 SUCTION SPECIFIC SPEED STARTING METHOD

58 MAX. ALLOW. SOUND PRESS. LEVEL REQD (6.1.14) (dBA) SEE DRIVER DATA SHEET

59 EST MAX SOUND PRESS. LEVEL (dBA) INSULATION / TEMP. RISE CLASS

60 MAX. SOUND POWER LEVEL REQ'D (6.1.14) EXPLOSION PROOF CLASS

61 EST MAX SOUND POWER LEVEL DEGREE OF PROTECTION

62 EFFICIENCY CLASS

63 SPACE HEATER WHEN MOTOR ABOVE 22 kW

Motor

VTA

Open Valve (Fully-Loaded)

85 (@1m) Note-21

REQUIRED

MOTOR

YES

50Hz 50Hz 50Hz

PERFORMANCE (VTC) DRIVER (7.1.5)

11000 230 230

3 1 1

DRIVERS HEATING CONTROL SHUTDOWN

2

T3

DRIVERS HEATING

GRADE TROPICALISATION REQD

SITE AND UTILITY DATA

OUTDOOR UNHEATED UNDER ROOF INLET RETURN DESIGN

DIFFERENTIAL HEAD : m

barg

DIFFERENTIAL PRESSURE : bar

HYDRAULIC POWER : kW

NPSHA : m

N/A

C.L. Impeller

Refer Page-11

o C

Units Maximum Rated Normal Minimum

Refer Page-11

m3/hr

barg

PROPOSAL API-610, 11th edition

Petrozim Line (PVT) Limited P-201/202

RELATIVE DENSITY :

VTA2 (1W + 1S)

Diesel/Petrol/Jet Fuel

LIQUID CHARACTERISTICS

Units

bara

II A

Wilton Pump Station Diesel/Petrol/Jet Fuel

Horizontal VTA (Multi-stage)

VTA VTA VTA

kJ/(kg-C) N/A

N/A

OPERATING CONDITIONS (6.1.2) - Case-1 N/A

cP




1 Rev

2 API PUMP TYPE: [Based on API 610 definitions] - Remark 5.4 CASING MOUNTING:

3 CASING TYPE: (6.3.10)

4 NOZZLE CONNECTIONS: (6.5.5) OH3 BACKPULLOUT LIFTING DEVICE REQD. (9.1.2.6)

5 CASE PRESSURE RATING:

6 SUCTION MAWP : (6.3.6) barg @ o C

7 DISCHARGE HYDROTEST : (1.5 X MAWP) barg @ o C

8 PRESSURE CASING AUX. CONNECTIONS: (6.4.3.2) - VTA

9 HYDROTEST OH PUMP AS ASSEMBLY

10 BALANCE/LEAK OFF SUCT'N PRESS. REGIONS DESIGNED FOR MAWP

11 DRAIN ROTATION: (VIEWED FROM COUPLING END)

12 VENT • IMPELLERS INDIVIDUALLY SECURED :

13 PRESSURE GAGE • BOLT OH 3/4/5 PUMP TO PAD / FOUNDATION :

14 TEMP GAGE • PROVIDE SOLEPLATE FOR OH 3/4/5 PUMPS

15 WARM-UP LINE ROTOR:

16 SHAFT FLEXIBILITY INDEX (SFI) (9.1.1.3)

17 Drain Valve Supplied By First Critical Speed Wet (Multi stage pumps only)

18 DRAINS MANIFOLDED COMPONENT BALANCE TO ISO 1940 G2.5

19 VENT Valve Supplied By SHRINK FIT -LIMITED MOVEMENT IMPELLERS (9.2.2.3)

20 VENTS MANIFOLDED

21 THREADED CONS FOR PIPELINE SERVICE & < 50°C (6.4.3.2) COUPLING:(7.2.3) (7.2.13.f)

22 SPECIAL FITTINGS FOR TRANSITIONING (6.4.3.3) MANUFACTURER

23 CYLINDRICAL THREADS REQUIRED (6.4.3.8) MODEL

24 GUSSET SUPPORT REQUIRED RATING (POWER/100 RPM)

25 MACHINED AND STUDDED CONNECTIONS (6.4.3.12) SPACER LENGTH mm

26 VS 6 DRAIN SERVICE FACTOR

27 DRAIN TO SKID EDGE RIGID

28 COUPLING WITH HYDRAULIC FIT (7.2.10)

29 COUPLING BALANCED TO ISO 1940-1 G6.3 (7.2.3)

30 APPENDIX H CLASS COUPLING WITH PROPRIETARY CLAMPING DEVICE (7.2.11)

31 MIN DESIGN METAL TEMP (6.12.4.1) o C FLEXIBLE METALLIC- DRY COUPLING

32 REDUCED-HARDNESS MATERIALS REQ'D (6.12.1.12.1) COUPLING IN COMPLIANCE WITH (7.2.4)

33 Applicable Hardness Standard (6.12.1.12.3) COUPLING GUARD STANDARD PER (7.2.13.a)

34 BARREL : Window on Coupling Guard

35 CASE :

36 DIFFUSERS

37 IMPELLER : API BASEPLATE NUMBER :

38 IMPELLER WEAR RING : BASEPLATE CONSTRUCTION (7.3.14)

39 CASE WEAR RING : BASEPLATE DRAINAGE (7.3.1)

40 SHAFT: MOUNTING :

41 Bowl (if VS-type) NON-GROUT CONSTRUCTION : (7.3.13)

42 Inspection Class VERTICAL LEVELING SCREWS :

43

44 LONGITUDINAL DRIVER POSITIONING SCREWS :

45 BEARING (TYPE / NUMBER): (6.11.4) SUPPLIED WITH : m GROUT AND VENT HOLES

46 RADIAL / l DRAIN CONNECTION

47 THRUST / MOUNTING PADS SIZED FOR BASEPLATE LEVELING (7.3.5)

48 REVIEW AND APPROVE THRUST BEARING SIZE : (9.2.5.2.4) MOUNTING PADS TO BE MACHINED (7.3.6)

49 PROVIDE SPACER PLATE UNDER ALL EQUIPMENT FEET

50 LUBRICATION : (6.10.2.2) (6.11.3) (9.6.1) OTHER

51 PRESSURE LUBE SYSTEM TO ISO 10438- (9.2.6.5)

52 ISO 10438 DATA SHEETS ATTACHED

53 Pressurized Lube Oil System mtd on pump baseplate REMARKS :

54 Location of Pressurized Lube Oil System mounted on baseplate :

55

56 INTERCONNECTING PIPING PROVIDED BY 5.2: Hydrodynamic Bearings with Pressurized Lube Oil System are considered. Vendor to check

57 and confirm as per Engery Density Limits (API-610 Table 10).

58 OIL VISC. ISO GRADE VG 5.3: Spacer Length shall be greater than Total Seal Length in compliance to API 610.

59 CONSTANT LEVEL OILER : 5.4: Pump type BB2 (if offered) shall be with Side-Side Nozzles Configuration.

Hydrodynamic

REQUIRED

RING OIL

or low alloy steel and 0 mm for high alloy steel or non-ferrous metal.

5.1: The pressure containing parts shall have a corrosion allowance of 3 mm for carbon

YES

STA

RF 900

YES

BASEPLATE

A216 Gr WCB

YES

4140 ALLOY STEEL

REQUIRED

REQUIRED

Entire Baseplate Drain Pan

A216 Gr WCB

BEARINGS AND LUBRICATION (6.10.1.1) REQUIRED

STA

NO STA

YES STA

YESSUPPLIER

YES YES

SUPPLIER YES

YES

NO

NO STA

NO API 610 compliant

YES

A216 Gr WCB

NO

N/A 1.5 Min.

S-5

5 YES

MATERIAL (6.12.1.1)

YES

STA STA WN RF 900 STA

CONSTRUCTION

CENTERLINE

Size Facing Rating Position

BB1 or BB2

Size Type Facing Rating Posn.

VTA RF 900 SIDE

ASTM A 743 CA6NM (H)

ASTM A 743 CA6NM (H)

Hydrodynamic

Axially Split

Remark 5.3

Brass

YES

VTA

YES

STA STA WN RF 900

SIDE

No.

STA




1 Rev

2 SEE ATTACHED API-670 DATA SHEET SEAL SUPPORT SYSTEM MOUNTED ON PUMP BASEPLATE

3 ACCELEROMETER (7.4.2.1) (7.5.1.4)

4 Number of Accelerometers IDENTIFY LOCATION ON BASEPLATE

5 Mounting Location of Accelerometers

6 INTERCONNECTING PIPING BY

7 PROVISION FOR MTG ONLY (6.10.2.10)

8 Number of Accelerometers

9 Mounting Location of Accelerometers SEE ATTACHED ISO 21049/API 682 DATA SHEET

10 ADDITIONAL CENTRAL FLUSH PORT (6.8.9)

11 FLAT SURFACE REQUIRED (6.10.2.11) HEATING JACKET REQ'D. (6.8.11)

12 Number of Accelerometers

13 Mounting Location of Accelerometers

14 COOLING REQ'D

15 VIBRATION PROBES (7.4.2.2) COOLING WATER PIPING PLAN

16 PROVISIONS FOR VIB. PROBES COOLING WATER PIPING

17 NUMBER PER RADIAL BEARING (Remark 6.2) FITTINGS

18 NUMBER PER AXIAL BEARING COOLING WATER PIPING MATERIALS

19 COOLING WATER REQUIREMENTS:

20 MONITORS AND CABLES SUPPLIED BY (7.4.2.4) BEARING HOUSING m3/hr

21 HEAT EXCHANGER m3/hr

22 TEMPERATURE (7.4.2.3) TOTAL COOLING WATER m3/hr

23 PROVISIONS FOR TEMP PROBES HEATING MEDIUM

24 RADIAL BEARING TEMP. OTHER

25 NUMBER PER RADIAL BEARING HEATING PIPING

26 THRUST BEARING TEMP.

27 NUMBER PER THRUST BEARING ACTIVE SIDE

28 NUMBER PER THRUST BEARING INACTIVE SIDE MANIFOLD PIPING FOR PURCHASER CONNECTION (7.5.1.6)

29 TEMP. GAUGES (WITH THERMOWELLS) (9.1.3.6) VENT

30 PRESSURE GAUGE TYPE DRAIN

31 Remarks COOLING WATER

32 TAG ALL ORIFICES (7.5.2.4)

33 SOCKET WELD CONN ON SEAL GLAND (7.5.2.8)

34

35

36

37 6.5: Mechanical seal shall be in compliance with API 682 with cartridge design.

38 6.6: If cooling system is required, shall be by air cooled.

39

40

41

42

43

44

Yes

N/A

YES

YES

YES

2

Pump Vendor

N / A

YES

Remark 6.6

INSTRUMENTATION SEAL SUPPORT SYSTEM MOUNTING

Supplier

YES

PIPING & APPURTENANCES2

N / A

YES

NO6.1: RTDs shall be duplex type

6.2: Vendor to provide 2 vibration probes for each radial bearing.

6.3: Vendor to provide Axial Position Probes in compliance to API 670.

6.4: Vendor to provide filled/completed API-670 datasheet during detailed engg.

Yes

SEPARATE CONSOLE INSTALLED NEAR PUMP BASE PLATE

YES

2

MECHANICAL SEAL (6.8.1) - Remark 6.5

HEATING AND COOLING (6.1.17)




1 Rev

2 MANUFACTURER'S STANDARD SHOP INSPECTION (8.1.1)

3 OTHER (SEE BELOW) PERFORMANCE CURVE

4 SPECIFICATION NO. & DATA APPROVAL PRIOR TO SHIPMENT.

5 TEST WITH SUBSTITUTE SEAL (8.3.3.2.b)

6 PUMP: MATERIAL CERTIFICATION REQUIRED CASING

7 PUMP SURFACE PREPARATION (6.12.1.8) IMPELLER

8 PRIMER SHAFT

9 FINISH COAT OTHER Remark 7.1

10 CASTING REPAIR WELD PROCEDURE APPR REQD

11 BASEPLATE: (6.12.2.5) (6.12.3.1)

12 BASEPLATE SURFACE PREPARATION INSPECTION REQUIRED FOR CONNECTION WELDS (6.12.3.4.d)

13 PRIMER: (6.12.3.4.e) MAG PARTICLE

14 FINISH COAT RADIOGRAPHY

15 DETAILS OF LIFTING DEVICES LIQUID PENETRANT

16 ULTRASONIC

17 SHIPMENT: (8.4.1) INSPECTION REQUIRED FOR CASTINGS

18 EXPORT BOXING REQUIRED MAG PARTICLE

19 OUTDOOR STORAGE MORE THAN 6 MONTHS RADIOGRAPHY

20 LIQUID PENETRANT

21 SPARE ROTOR ASSEMBLY PACKAGED FOR: ULTRASONIC

22 ROTOR STORAGE ORIENTATION (9.2.8.2) HARDNESS TEST REQUIRED (8.2.2.7)

23 SHIPPING & STORAGE CONTAINER FOR VERT STORAGE (9.2.8.3) ADDNL SUBSURFACE EXAMINATION (6.12.1.5) (8.2.1.3)

24 FOR

25 N2 PURGE (9.2.8.4) METHOD

26 SPARE PARTS PMI TESTING REQUIRED (8.2.2.8)

27 START-UP COMPONENTS TO BE TESTED

28 NORMAL MAINTENANCE

29 WEIGHTS (kg) -VTC RESIDUAL UNBALANCE TEST (J.4.1.2)

30

31 NOTIFICATION OF SUCCESSFUL SHOP

32 PERFORMANCE TEST (8.1.1.c) (8.3.3.5)

33 BASEPLATE TEST (7.3.21)

34 HYDROSTATIC

35 HYDROSTATIC TEST OF BOWLS & COLUMN (9.3.13.2)

36 PERFORMANCE TEST

37 COORDINATION MEETING REQUIRED (10.1.3) TEST IN COMPLIANCE WITH (8.3.3.2)

38 MAXIMUM DISCHARGE PRESSURE TO INCLUDE TEST DATA POINTS TO (8.3.3.3)

39 MAX RELATIVE DENSITY TEST TOLERANCES TO (8.3.3.4)

40 OPERATION TO TRIP SPEED NPSH (8.3.4.3.1) (8.3.4.3.4)

41 MAX DIA. IMPELLERS AND/OR NO OF STAGES NPSH-1ST STG ONLY (8.3.4.3.2)

42 CONNECTION DESIGN APPROVAL (9.2.1.4) NPSH TESTING TO HI 1.6 OR ISO 9906 (8.3.4.3.3)

43 TORSIONAL ANALYSIS / REPORT (6.9.2.10) TEST NPSHA LIMITED TO 110% SITE NPSHA (8.3.3.6)

44 PROGRESS REPORTS RETEST ON SEAL LEAKAGE (8.3.3.2.d)

45 OUTLINE OF PROC FOR OPTIONAL TESTS (10.2.5) RETEST REQUIRED AFTER FINAL HEAD ADJ (8.3.3.7.b)

46 ADDITIONNAL DATA REQUIRING 20 YEARS RETENTION (8.2.1.1) COMPLETE UNIT TEST (8.3.4.4.1)

47 SOUND LEVEL TEST (8.3.4.5)

48 LATERAL ANALYSIS REQUIRED (9.1.3.4) (9.2.4.1.3) VTA CLEANLINESS PRIOR TO FINAL ASSEMBLY (8.2.2.6)

49 MODAL ANALYSIS REQUIRED (9.3.9.2) LOCATION OF CLEANLINESS INSPECTION

50 DYNAMIC BALANCE ROTOR (6.9.4.4) NOZZLE LOAD TEST

51 INSTALLATION LIST IN PROPOSAL (10.2.3.l) CHECK FOR CO-PLANAR MOUNTING PAD SURFACES

52 VFD STEADY STATE DAMPED RESPONSE ANALYSIS (6.9.2.3) MECHANICAL RUN TEST UNTIL OIL TEMP STABLE

53 4 HR. MECH RUN AFTER OIL TEMP STABLE (8.3.4.2.1)

54 TRANSIENT TORSIONAL RESPONSE (6.9.2.4) 4 HR. MECH RUN TEST (8.3.4.2.2)

55 BEARING LIFE CALCULATIONS REQUIRED (6.10.1.6)

56 IGNITION HAZARD ASSMT TO EN 13463-1 (7.2.13.e) BRG HSG RESONANCE TEST (8.3.4.7)

57 CASING RETIREMENT THICKNESS DRAWING (10.3.2.3) STRUCTURAL RESONANCE TEST (9.3.9.2)

58 FLANGES RQD IN PLACE OF SKT WELD UNIONS (7.5.2.8) REMOVE / INSPECT HYDRODYNAMIC BEARINGS AFTER TEST

59 INCLUDE PLOTTED VIBRATION SPECTRA (6.9.3.3) (9.2.7.5)

60 CONNECTION BOLTING (7.5.1.7) AUXILIARY EQUIPMENT TEST (8.3.4.6)

61 CADMIUM PLATED BOLTS PROHIBITED EQUIPMENT TO BE INCLUDED IN AUXILLIARY TESTS

62 VENDOR TO KEEP REPAIR AND HT RCDS (8.2.1.1.c)

63 VENDOR SUBMIT TEST PROCEDURES (8.3.1.1) LOCATION OF AUXILIARY EQUIPENT TEST

64 SUBMIT INSPECTION CHECK LIST (8.1.5)

65 IMPACT TEST (6.12.4.3) PER EN 13445

66 Remarks PER ASME SECTION VIII

67 REMOVE CASING AFTER TEST

YES

WIT

8.3.3.2

8.3.3.3

OTHER PURCHASER REQUIREMENTS WIT

YES

Table 16

YES

SS

YES Seal System

YES

7.1: Pressure containing parts

YES

WIT

YES

YES

YES

YES

WIT

YES

YES

YES

WIT

YES

YES

ITEM No PUMP DRIVER GEAR BASE

YES

YES

YES

YES

YES

VTA YES

YES

VTA YES

VTA

YES

VTA

VTA

YES

YES

YES

YES

SURFACE PREPARATION AND PAINT TEST

YES YES

YES

VTA

VTA YES

WIT

TOTAL




1 Note Rev

2 THESE REFERENCES MUST BE LISTED BY THE MANUFACTURER

3 CASTING FACTORS USED IN DESIGN ( TABLE 4)

4 SOURCE OF MATERIAL PROPERTIES

5

6

7 THESE REFERENCES MUST BE LISTED BY THE PURCHASER. (DEFAULT TO TABLE 11 IF NO PURCHASER PREFERENCE IS STATED)

8 ALTERNATE WELDING CODES AND STANDARDS

9 WELDING REQUIREMENT (APPLICABLE CODE OR STANDARD)

10 WELDER/OPERATOR QUALIFICATION

11 WELDING PROCEDURE QUALIFICATION

12 NON-PRESSURE RETAINING STRUCTURAL WELDING SUCH AS BASEPLATES OR SUPPORTS

13 MAGNETIC PARTICLE OR LIQUID PENETRANT EXAMINATION OF PLATE EDGES

14 POSTWELD HEAT TREATMENT

15 POSTWELD HEAT TREATMENT OF CASING FABRICATION WELDS

16

17

18 THESE REFERENCES MUST BE LISTED BY THE PURCHASER DEFAULT TO TABLE 14

19 ALTERNATIVE MATERIAL INSPECTIONS AND ACCEPTANCE CRITERIA (SEE TABLE 14) (8.2.2.5)

20

21 RADIOGRAPHY

22 ULTRASONIC INSPECTION

23 MAGNETIC PARTICLE INSPECTION

24 LIQUID PENETRANT INSPECTION

25 VISUAL INSPECTION (all surfaces)

26

27 REMARKS :

28

29

30

31

32

33

34

35

36

37

38

39

40

41

42

43

44

45

46

47

48

49

50

51

52

53

54

55

56

57

58

59

60

TABLE 15 (8.2.2.5)

TABLE 15 (8.2.2.5)

TYPE OF INSPECTION METHOD FOR FABRICATIONS FOR CASTINGS

TABLE 15 (8.2.2.5)

YES

MATERIAL INSPECTION

AS PER TABLE 11 of API 610 11th Ed.


TABLE 15 (8.2.2.5)

TABLE 15 (8.2.2.5)

PRESSURE VESSEL DESIGN CODE REFERENCES

WELDING AND REPAIRS

YES









1 DATA SUPPLIED CUSTOMARY UNITS SI UNITS HARDWARE SUPPLIED CUSTOMARY UNITS SI UNITS

2 INDICATES DATA COMPLETED BY PURCHASER BY SEAL VENDOR BY SEAL VENDOR OR PURCHASER

3 DEFAULT SELECTION

4

5 CATEGORY SEAL CATEGORY 1 (4.1.1) SEAL CATEGORY 2 (4.1.1) SEAL CODE (ANNEX J)

6 TYPE TYPE A (4.1.3) TYPE B (4.1.3) ALTERNATIVE STATIONARY (TYPE A & B)

7 (CODE-CW) TYPE C (4.1.3) ALTERNATIVE ROTATING (TYPE C) SINGLE SPRING (TYPE A)

8

9 1 (4.1.4.1) 1CW-FX 1CW-FL DIST. FLUSH 01 11 14 23 32 50 61

10 ALTERNATIVE BUSH 02 13 21 31 41 51 65

11 LIQUID 2CW-CW FX DIST. FLUSH 01 13 23 41 62 75

12 2 (4.1.4.1) TANGENTIAL LBO CONN'N 02 14 31 52 71 76

13 GAS 2CW-CS 2NC-CS FX DIST. FLUSH 11 21 32 61 72 65

14 LIQUID 3CW-FB 3CW-BB FX 01 13 53A 54 74

15 3 (4.1.4.1) 3CW-FF TANG. LBO 02 14 53B 61

16 GAS 3NC-BB 3NC-FF 3NC-FB 11 32 53C 62

17 SLEEVE-SHAFT DRIVE SET-SCREW ONTO SHAFT ALTERNATIVE (6.1.3.13) - SPECIFY

18

19 SECONDARY SEALS SEAL FACES METAL BELLOWS SPRINGS METAL PARTS

20 FKM FFKM CARBON VS SIC UNS N10276 (TYPE B) UNS N10276 UNS S31600/ S31635

21 SPIRAL-W GASKET SIC VS SIC UNS N07718 (TYPE C) OR N06455 UNS N10276

22 NBR SS-SIC RB-SIC UNS N08020 UNS S31600 UNS N08020

23 OTHER: VS OTHER: OR S31635 OTHER:

24

25 SEAL VENDOR ALTERNATIVE SEAL FOR PUMP PERFORMANCE TEST

26 DATA REQUIREMENTS FORM (ANNEX E) DYNAMIC SEALING PRESSURE RATING (3.1.27) bar (g)

27 SIZE/TYPE STATIC SEALING PRESSURE RATING (3.1.55) bar (g)

28 SEAL DRAWING NUMBER MAXIMUM ALLOWABLE TEMPERATURE (3.1.51) 85oC

29 VENDOR'S SEAL CODE MINIMUM DESIGN METAL TEMPERATURE (6.1.6.11.1) 4oC

30 MODIFIED FACES FOR PUMP PERFORMANCE TEST

31

32 ASME B73.1 & 2 CYLINDRICAL TAPERED ISO 13709 ISO 3069-C OTHER, SPECIFY

33 BOLT-ON CHAMBER (6.1.2.5) SEAL CHAMBER FLUSH PORT REQ'D SEAL CHAMBER VENT REQ'D

34 FLOATING THROAT BUSH FIXED THROAT BUSH CHAMBER HEATING REQ'D

35

36 PUMP DESIGN MANUFACTURER MODEL FRAME/SIZE CASE MATERIAL

37 PUMP OPERATING PRESSURE SUCTION PRESS. (RATED) bar (g) DISCHARGE PRESSURE bar (g)

38 SEAL CHAMBER NORMAL bar (g) MIN / MAX / bar (ga) MSSP (3.1.55) bar (g)

39 SHAFT HORIZONTAL VERTICAL DIA. mm SHAFT SPEED r/min

40 SHAFT DIRECTION (FROM DRIVER): CW CCW

41

42 PUMPED STREAM (REFER PAGE 4 & 11) HAZARDOUS FLAMMABLE

43 TYPE OR NAME CONC'N % FLUID SOLID @ AMBIENT

44 DISSOLVED CONTAMINANT H2S ml/m3

WET SOLIDIFIES @ °C POUR POINT °C

45 Cl2 ml/m3

OTHER @ ml/m3

PUMPED STREAM SOLIDIFIES UNDER SHEAR

46 SOLID CONTAMINANT PUMPED STREAM CONTAINS AGENTS THAT POLYMERIZE

47 CONCENTRATION (MASS FRACTION) SPECIFY AGENTS @ TEMP °C

48 PUMPING TEMPERATURE PUMPED STREAM CAN PLATE OUT OR DECOMPOSE:

49 MIN °C NORMAL °C MAX °C SPECIFY CONDITIONS

50 RELATIVE DENSITY (TO WATER @ 25°C) AT REF. TEMP. PUMPED STREAM IS REGULATED FOR FUGITIVE OR

51 @ NORMAL TEMP @ MAX TEMP OTHER EMISSIONS. REGULATION LEVEL ml/m3

52 ABSOLUTE VAPOR PRESSURE AT REFERENCE TEMP. SPECIAL PUMP CLEANING PROCEDURES

53 NORMAL TEMP bar MAX TEMP bar SPECIFY;

54 ATMOSPHERIC BOILING POINT. °C ALTERNATIVE PROCESS FLUIDS & CONCENTRATION

55 VISCOSITY @ NORMAL PUMPING TEMP. cP (INCL. COMMISIONING)

56 FLUSH FLUID (PLAN 32)

57 TYPE OR NAME CONC'N % ABSOLUTE VAPOR PRESSURE AT REFERENCE TEMP.

58 SEAL VENDOR REVIEW REQUIRED NORMAL TEMP bar MAX TEMP bar

59 FLUID TEMPERATURE ATMOSPHERIC BOILING POINT. °C

60 MIN °C NORMAL °C MAX °C VISCOSITY @ NORMAL PUMPING TEMP. Pa.s

61 RELATIVE DENSITY (TO WATER @ 25°C) AT REF. TEMP. FLOW RATE REQ'D MAX/MIN / l/min

62 @ NORMAL TEMP @ MAX TEMP PRESSURE REQ'D MAX/MIN / bar (ga)

63

MATERIALS (REFERENCE 6.1.6 & ANNEX B)

MECHANICAL SEAL DATA

SEAL CHAMBER DATA (REFERENCE 6.1.2.4)

PUMP DATA - REFER TO SHEETS 2

FLUID DATA

BA

RR

IER

CATEGORY 1 & 2 SEALS

MECHANICAL SEAL DATA SHEET: API 682 4th EDITION

SEAL SPECIFICATION - (REF CLAUSE 4.1, FIGURES 1 TO 9)

ARR'G'T DEFAULT CONFIGURATION ALTERNATIVE DESIGN FLUSH PLANS (SEE ANNEX G)

BU

FF

ER




1 INDICATES DATA COMPLETED BY PURCHASER BY SEAL VENDOR BY SEAL VENDOR OR PURCHASER

2 DEFAULT SELECTION

3 FLUID DATA - (QUENCH, BUFFER AND BARRIER FLUID DATA, LIQUID AND GAS)

4 QUENCH MEDIUM (PLAN 51, 62) SUPPLY TEMPERATURE MAX/MIN / °C

5 TYPE OR NAME FLOW RATE REQ'D MAX/MIN / l/min

6 BUFFER/BARRIER MEDIUM

7 TYPE OR NAME RELATIVE DENSITY (TO WATER @ 25°C) AT REF. TEMP.

8 PURCHASER SELEC'N SEAL VENDOR SELEC'N @ NORMAL TEMP @ MAX TEMP

9 SEAL VENDOR REVIEW PURCHASER REVIEW ABSOLUTE VAPOR PRESSURE AT REFERENCE TEMP.

10 FLOW RATE REQ'D MAX/MIN. / l/min NORMAL TEMP bar MAX TEMP bar

11 COOLING/HEATING REQUIRED (+ OR -) Kw ATMOSPHERIC BOILING POINT (LIQUID) °C

12 SUPPLY PRESSURE MAX/MIN. / bar (ga) VISCOSITY @ NORMAL TEMP (LIQUID) Pa.s

13 FLUID OPERATING TEMPERATURE SPECIFIC HEAT CAPACITY @ CONSTANT PRESSURE

14 MIN °C NORMAL °C MAX °C FOR LIQUID @ NORMAL TEMPERATURE J/Kg.K

15 SITE AND UTILITIES (RFER PROCESS DESIGN BASIS 14.99.91.0631 AND UTILITY AND CHEMICAL SUMMERY 14.99.91.0657)

16 CONTROL VOLTAGE V PHASE HERTZ COOLING H2O SUPPLY TEMP. °C Cl2 ml/m3

17 ELECTRICAL AREA CL GR DIV COOLING H2O PRESS. NORM./DES. / bar (ga)

18 DESIGN AMBIENT MIN./MAX. / °C ATEX (EC DIRECTIVE 94/9/EC) GR CAT. T CLASS

19 ACCESSORIES

20 GENERAL PLAN 52 AND 53 SYSTEMS CONTINUED

21 JOINT USER/VENDOR LAYOUT OF EQUIPMENT (8.1.3) EQUIPMENT SUPPORT SUPPLIER

22 PIPE TAPER THREADS (8.2.13) ISO 7 ASME B1.20.1 FILLING SYSTEM SUPPLIER

23 SPECIAL REQUIREMENTS FOR HAZARDOUS SERVICE ASME CODE STAMP REQUIRED

24 EN 13445 OR OTHER CODE APPLICABLE

25 RESERVOIR CAPACITY (8.3.6.2.5) l

26 UTILITY MANIFOLD CONNECTIONS REQUIRED (8.2.24) NLL TO GLAND PLATE HEIGHT (8.3.6.2.2) m

27 TYPE AND SPEC. OF HEAT TRACING (8.2.23) RESERVOIR MAWP bar (ga) @ °C

28 SET PRESSURE RANGE, MAX/MIN / bar (ga)

29 THERMAL RELIEF VALVES REQUIRED (9.8.3) SYSTEM HOLD-UP PERIOD (PLANS 53B & 53C) DAYS

30 COOLING SYSTEM (PLAN 21, 22, 23, 41, 53B, 53C) TEMPERATURE INDICATOR (PLAN 53B & 53C)

31 HEAT EXCHANGER SUPPLIER PRESSURE SWITCH TO ACTIVATE ON;

32 WATER COOLED AIR COOLED ISO 15649 RISING PRESSURE (ARR 2) SET @ bar (ga)

33 EQUIPMENT REFERENCE/CODE FALLING PRESSURE (ARR 3) SET @ bar (ga)

34 COOLING WATER LINES SUPPLIER HIGH LEVEL ALARM REQUIRED (8.3.6.2.4)

35 TUBING SS 316 L PIPING (8.2.21) TEST BASED H/Q CURVE FOR INTERNAL CIRC. DEVICE

36 COOLING WATER FLOW RATE l/min EXTERNAL CIRCULATING PUMP (8.3.7)

37 SIGHT FLOW INDICATORS (8.2.22) OPEN CLOSED PLAN 72 AND 74 SYSTEM

38 PLAN 11, 13, 14, 21, 23, 31, 32 AND 41 SYSTEMS EQUIPMENT SUPPLIER

39 CONNECTING LINES SUPPLIER HIGH FLOW ALARM SWITCH

40 TUBING PIPING (8.2.9) PLAN 75 AND 76 SYSTEM

41 RESTRICTION ORIFICE NIPPLE IN FLUSH LINE (8.3.5.4) EQUIPMENT SUPPLIER

42 CYCLONE SEPARATOR SUPPLIER HIGH LEVEL ALARM SWITCH FOR PLAN 75 (8.3.9.3.3)

43 PLAN 32 EQUIPMENT SUPPLIER TEST CONNECTION (8.3.9.3.4)

44 PLAN 32 FLOW IND'R PLAN 32 TEMPERATURE IND'R INSTRUMENTATION

45 PLAN 52 AND 53 SYSTEMS USER SPECIFICATION REFERENCE FOR

46 STANDARD (Appendix F.3) ALTERNATIVE (Appendix F.3) INSTRUMENTATION/CONTROLS

47 DIMENSIONAL VARIATIONS TO STANDARD ( F.3 ) PRESSURE GAUGES (9.4);

48 OIL FILLED PRESSURE GAUGES (9.4.3)

49 DIMENSIONAL VARIATIONS TO ALTERNATIVE ( F.3 ) PRESSURE SWITCHES (9.5.2); TRANSMITTER (9.5.2.1)

50 LEVEL SWITCHES (9.5.3); TRANSMITTER (9.5.3)

51 ALTERNATIVE FABRICATION STANDARD HYDROSTATIC CAPACITANCE ULTRASONIC

52 PRIMARY EQUIPMENT SUPPLIER LEVEL INDICATORS (9.6)

53 SUPPLIER REFERENCE/CODE WELD PAD EXTERNAL, REMOVABLE (9.6.2)

54 CONNECTING LINES SUPPLIER FLOW INSTRUMENTS (9.7); TRANSMITTER (9.7)

55 TUBING SCH 80 PIPING (8.2.9)

56 INSPECTION AND TESTING

57 PURCHASER PARTICIPATION IN INSPECTION & TEST 100% INSPECTION OF ALL WELDS (6.1.6.10.5) USING;

58 SPECIFY; YES MAGNETIC PARTICLE LIQUID PENETRANT

59 INSPECTOR'S CHECK LIST (10.1.7 & ANNEX H) RADIOGRAPHIC ULTRASONIC

60 PURCHASER APPROVAL REQUIRED FOR WELDED OPTIONAL QUALIFICATION TESTING REQ'D (10.3.2)

61 CONNECTION DESIGNS, (6.1.6.10.5) MOD. FACES FOR PUMP TEST, SEE PG 1, LINE 30

62 HARDNESS TEST (10.2.3 k) REQUIRED FOR; ALTERNATIVE SEAL PUMP TEST, SEE PG 1, LINE 25

63

CATEGORY 1 & 2 SEALS

MECHANICAL SEAL DATA SHEET: API 682 4th EDITION




Rev

1) VENDOR TO REFER FOLLOWING LIQUID CHARACTERISTICS AND OPERATING CONDITIONS FOR DIESEL, PETROL AND JET FUEL:

a)

VAPOR PRESSURE :

SPECIFIC HEAT :

KINEMATIC VISCOSITY :

NPSHa Datum:

PUMPING TEMPERATURE :

FLOW :

DISCHARGE PRESSURE : (6.3.2)

SUCTION PRESSURE :

a)

VAPOR PRESSURE :

SPECIFIC HEAT :


NPSHa Datum:


FLOW :


SUCTION PRESSURE :

b)

VAPOR PRESSURE :

SPECIFIC HEAT :


NPSHa Datum:


FLOW :


SUCTION PRESSURE :

2) PROCESS DESIGN PRESSURE IS BASED ON SUM OF MAXIMUM SUCTION PRESSURE AND PUMP SHUT-OFF PRESSURE FOR PETROL AT MAXIMUM SPEED. SHUT-OFF PRESSURE SHALL NOT EXCEED 99.6 BARG WHICH IS THE

EXISTING PIPELINE DESIGN PRESSURE. VENDOR TO ENSURE SHUT-OFF PRESSURE WITHIN LIMITS FOR DIESEL & JET FUEL SERVICES AS WELL.

3) VENDOR TO SELECT PUMP, MOTOR AND VSD TO COVER ENTIRE RANGE OF OPERATION FOR DIESEL, PETROL AND THE JET FUEL CONSIDERING MAX. SUCTION PRESSURE FOR EACH CASE.

4) PUMP MINIMUM STABLE FLOW TO BE CONFIRMED BASED ON SELECTED VENDORS PUMP DATA.

5) PUMP SHALL COMPLY WITH THE REQUIREMENTS OF TECHNICAL SPECIFICATION FOR PUMPS (DOC. NO. 19911-ME-SPC-CMN-0001) AND API 610 (11TH EDITION).

6) SUPPLIER SHALL PROVIDE A PUMP WITH NPSHR LESS THAN NPSHA BY AT LEAST 1M AT RATED FLOW AND MINIMUM 0.5M AT 120% AT BEST EFFICIENCY POINT FOR EACH FLUID (DIESEL, PETROL AND JET FUEL). IN CASE NPSH MARGIN IS

LESS THAN 1.0 M AT RATED POINT, NPSH TEST (WITNESS) SHALL BE REQUIRED.

7) VENDOR TO PROVIDE PERFORMANCE CURVES FOR EACH FLUID (DIESEL, PETROL AND JET FUEL) DURING BIDDING AND DETAILED ENGINEERING.

8) RATED IMPELLER DIAMETER SHALL NOT BE MORE THAN 90% OF THE MAXIMUM IMPELLER SIZE POSSIBLE WITHIN THE PUMP CASING.

9) PUMP EFFICIENCY SHALL BE GREATER THAN 75% (HIGHEST POSSIBLE EFFICIENCY). PUMP EFFICIENCY SHALL INCLUDE ALL LOSSES INCLUDING MECHANICAL SEAL LOSS.

10) ALLOWABLE NOZZLE LOADS AND MOMENTS SHALL BE TWICE THE VALUES STATED IN API 610.

11) MECHANICAL SEAL MANUFACTURER TO CHECK/CONFIRM MECHANICAL SEAL TYPE AND ARRANGEMENT. PLAN 11 WITH PLAN 65 FOR LEAK DETECTION SYSTEM IS PROPOSED. PUMP/SEAL VENDOR TO CHECK AND CONFIRM FOR THE

APPLICATION AND IF REQUIRED, VENDOR TO OFFER ALTERNATE MECHANICAL SEAL AND PIPING PLAN DURING BIDDING.

12) THE FACES OF MECHANICAL SEAL SHALL BE SUITABLE FOR ALL THE LIQUIDS COMPOSITION.

13) DYNAMIC AND STATIC SEALING PRESSURE RATING SHALL BE AS PER API 682.

NOTES

LIQUID CHARACTERISTICS (Diesel)

LIQUID TYPE OR NAME : Units Diesel

TEMPERATURE: o C 37 15 5

bara 0.67 0.28 0.0007

cS 2.1 2.9 3.5

RELATIVE DENSITY : 0.82 0.835 0.87

kJ/(kg-C) NA NA NA

C.L. Impeller

o C 37 37 15 5

RATED CONDITIONS - (DIESEL)


m3/hr 607 180(Note-4)

barg 75.38

DIFFERENTIAL HEAD : m 867

barg 10.93 3

DIFFERENTIAL PRESSURE : bar 72.38

HYDRAULIC POWER : kW 1725

NPSHA : m 40

LIQUID CHARACTERISTICS (PETROL)

LIQUID TYPE OR NAME : Units PETROL


bara 0.67 0.28 0.0007


kJ/(kg-C) NA NA NA

cS 0.55 0.6 0.7

C.L. Impeller

o C 37 37 15 5

RATED CONDITIONS - (PETROL)


m3/hr 621 180(Note-4)

barg 65


barg 23.44 3

DIFFERENTIAL PRESSURE : bar 62


NPSHA : m 46

LIQUID CHARACTERISTICS (JET FUEL)

LIQUID TYPE OR NAME : Units JET FUEL


bara 0.67 0.28 0.0007


kJ/(kg-C) NA NA NA

cS 1.36 1.80 2.08

C.L. Impeller

o C 37 37 15 5

RATED CONDITIONS - (JET FUEL)


m3/hr 618 180(Note-4)

barg 72.94


barg 14.43 3

DIFFERENTIAL PRESSURE : bar 69.94


NPSHA : m 41.2




Rev

14) ALL REQUIRED INTERCONNECTING PIPING AND CABLING BETWEEN THE MAIN PUMP SKID AND ACCESSORY EQUIPMENT SKIDS SHALL BE PROVIDED BY THE SUPPLIER.

15) THREADED, SOCKET WELDED, SLIP ON CONNECTION JOINTS SHALL NOT BE ALLOWED.VENDDOR TO USE FULL PENETRATION BUTT WELDS.

16) ALL PIPING FOR INTERFACE CONNECTIONS SHALL BE VALVED, FLANGED AND BROUGHT TO SKID EDGE.

17) INSTRUMENTATION & CONTROL SHALL BE PROVIDED AS PER SPECIFICATION FOR PACKAGE INSTRUMENTATION DOC. NO. 19911-IC-SPC-CMN-0006, SPECIFICATION FOR FIELD INSTRUMENTS DOC. NO. 19911-IC-SPC-CMN-0005

AND PROJECT DESIGN BASIS MEMORANDUM DOC. NO. 19911-EN-DBM-CMN-0001.

18) CONTROL AND SAFEGUARDING SHALL BE IMPLEMENTED FOR EACH PUMP THROUGH PLANT SCADA SYSTEM.

19) VENDOR TO PROVIDE COMPLETE DETAILS OF MACHINE MONITORING AND CONDITION MONITORING SYSTEMS AS APPLICABLE DURING BIDDING AND COMPLETED DATASHEET AS PER API-670 DURING DETAILED ENGG.

20) ELECTRICAL MOTOR SHALL BE SIZED TO COVER ENTIRE RANGE OF PUMP OPERATION UP TO END OF CURVE FOR EACH FLUID (DIESEL, PETROL AND JET FUEL).

21) MV MOTOR SHALL COMPLY WITH REQUIREMENTS IN SPECIFICATION FOR MOTOR (19911-EL-SPC-CMN-0006) AND DATA SHEET FOR MOTORS (19911-EL-DAT-CMN-0002). VENDOR SHALL FILL UP & SUBMIT DATA SHEET SEPARATE FOR

EACH MOTOR.

22) ELECTRICAL EQUIPMENT INSTALLED IN HAZARDUOUS AREA SHALL ALSO BE SUITABLE FOR ZONE 2, IIB, T3 CLASSIFICATION AND PROTECTION CATEGORY SHALL BE AS FOLLOWS:-

a) MV MOTOR - Exd , IIB , T3 , IP55 Exd,ATEX /IEC Ex DUAL CERTIFIED

b) JUNCTION / TERMINAL BOX -Ex-eb, IIB, T3, IP55 Exd,ATEX /IEC Ex DUAL CERTIFIED

c) LOCAL CONTROL STATION - Ex-eb,ATEX /IEC Ex DUAL CERTIFIED

23) PUMP-SETS WILL HAVE EMERGENCY DIESEL GENERATOR SET BACK-UP POWER SUPPLY (BY OTHERS)

24) A COMPLETE UNIT TEST SHALL BE CARRIED OUT FOR THE FIRST READY PUMP PACKAGE. ALL CONTRACT COMPONENTS AND ACCESSORIES THAT COMPRISE THE COMPLETE UNIT SHALL BE TESTED TOGETHER.

25) PUMP SET TO BE PAINTED IN ACCORDANCE WITH SUPPLIER STANDARD FOR AN OUTDOOR LOCATION. SUPPLIER TO PROVIDE DETAILS.

26) VENDOR SHALL SUPPLY FOUNDATION BOLTS ALONG WITH HOLD DOWN BOLTS FOR EACH PUMP.

NOTES

Project No. 19911 Detail Engineering & Procurement Support ...

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