project no. 19911 detail engineering & procurement support
TRANSCRIPT
Project No. 19911
Detail Engineering & Procurement Support Services for Feruka – Harare Pipeline Series Operation
Comments Resolution Sheet (CRS)
Page 1 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
DATA SHEET FOR MAINLINE PUMPS (API-610)-WILTON PUMP STATION
Document No. : 19911-ME-DAT-WIL-0001 Rev : 0
Project No. : 19911 Page : 4 OF 12
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
DATA SHEET FOR MAINLINE PUMPS (API-610)-WILTON PUMP STATION
Document No. : 19911-ME-DAT-WIL-0001 Rev : 0
Project No. : 19911 Page : 5 OF 12
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
DATA SHEET FOR MAINLINE PUMPS (API-610)-WILTON PUMP STATION
Document No. : 19911-ME-DAT-WIL-0001 Rev : 0
Project No. : 19911 Page : 6 OF 12
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)
DATA SHEET FOR MAINLINE PUMPS (API-610)-WILTON PUMP STATION
Document No. : 19911-ME-DAT-WIL-0001 Rev : 0
Project No. : 19911 Page : 7 OF 12
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
DATA SHEET FOR MAINLINE PUMPS (API-610)-WILTON PUMP STATION
Document No. : 19911-ME-DAT-WIL-0001 Rev : 0
Project No. : 19911 Page : 8 OF 12
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.
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
AS PER TABLE 11 of API 610 11th Ed.
AS PER TABLE 11 of API 610 11th Ed.
AS PER TABLE 11 of API 610 11th Ed.
AS PER TABLE 11 of API 610 11th Ed.
AS PER TABLE 11 of API 610 11th Ed.
DATA SHEET FOR MAINLINE PUMPS (API-610)-WILTON PUMP STATION
Document No. : 19911-ME-DAT-WIL-0001 Rev : 0
Project No. : 19911 Page : 9 OF 12
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
DATA SHEET FOR MAINLINE PUMPS (API-610)-WILTON PUMP STATION
Document No. : 19911-ME-DAT-WIL-0001 Rev : 0
Project No. : 19911 Page : 10 OF 12
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
DATA SHEET FOR MAINLINE PUMPS (API-610)-WILTON PUMP STATION
Document No. : 19911-ME-DAT-WIL-0001 Rev : 0
Project No. : 19911 Page : 11 OF 12
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 :
KINEMATIC VISCOSITY :
NPSHa Datum:
PUMPING TEMPERATURE :
FLOW :
DISCHARGE PRESSURE : (6.3.2)
SUCTION PRESSURE :
b)
VAPOR PRESSURE :
SPECIFIC HEAT :
KINEMATIC VISCOSITY :
NPSHa Datum:
PUMPING TEMPERATURE :
FLOW :
DISCHARGE PRESSURE : (6.3.2)
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)
Units Maximum Rated Normal Minimum
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
TEMPERATURE: o C 37 15 5
bara 0.67 0.28 0.0007
RELATIVE DENSITY : 0.71 0.73 0.76
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)
Units Maximum Rated Normal Minimum
m3/hr 621 180(Note-4)
barg 65
DIFFERENTIAL HEAD : m 853
barg 23.44 3
DIFFERENTIAL PRESSURE : bar 62
HYDRAULIC POWER : kW 1527
NPSHA : m 46
LIQUID CHARACTERISTICS (JET FUEL)
LIQUID TYPE OR NAME : Units JET FUEL
TEMPERATURE: o C 37 15 5
bara 0.67 0.28 0.0007
RELATIVE DENSITY : 0.76 0.8 0.84
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)
Units Maximum Rated Normal Minimum
m3/hr 618 180(Note-4)
barg 72.94
DIFFERENTIAL HEAD : m 864
barg 14.43 3
DIFFERENTIAL PRESSURE : bar 69.94
HYDRAULIC POWER : kW 1698
NPSHA : m 41.2
DATA SHEET FOR MAINLINE PUMPS (API-610)-WILTON PUMP STATION
Document No. : 19911-ME-DAT-WIL-0001 Rev : 0
Project No. : 19911 Page : 12 OF 12
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