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GENERAL ENGINEERING SPECIFICATION

ASME CENTRIFUGAL PUMPS

GES G.02

Page 2 of 21

Rev 0 1999

INDEX

SEC TITLE PAGE

1.0 SCOPE OF SPECIFICATION 4

1.1 Introduction 4

1.2 Other NOC Specifications 4

1.3 Data Sheets 5

2.0 DEFINITIONS 5

2.1 Technical 5

2.2 Contractual 5

3.0 DESIGN 6

3.1 Codes and Standards 6

3.2 Additions and Exceptions to

ASME B73.IM Horizontal Pumps 6

3.3 Additions and Exceptions to

ASME B73.2M Vertical Pumps 10

4.0 MATERIALS 14

4.1 ASME Requirements 14

4.2 H2S Corrosion 14

4.3 Miscellaneous 144.4 Mechanical Seals 15

5.0 INSPECTION 15

5.1 Procedures 15

5.2 Scope 16

5.3 Nameplates 16

6.0 TESTING 16

6.1 Required Tests 16

6.2 Test Requirements 17

6.3 Test Certificates 18

7.0 DOCUMENTATION 18

7.1 Introduction 18

7.2 Schedules and Reports 18

7.3 Data and Drawings 18

7.4 Manuals 19

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SEC TITLE PAGE

8.0 PRIOR TO SHIPMENT 19

8.1 Painting and Coatings 19

8.2 Spares 20

8.3 Packing and Storage 20

8.4 Shipping 20

8.5 Warranty 20

DATA SHEETS

ASME Form A1 Centrifugal Pump Data Sheet (1 sheet)

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1.0 SCOPE OF SPECIFICATION

1.1 Introduction

1.1.1 This specification gives the minimum requirements for the design, material selection, inspection, testing,

documentation and preparation for shipment of single horizontal end suction and vertical in-line centrifugal

pumps.

1.1.2 This specification applies mainly to pumps in non-flammable, non-toxic and auxiliary services e.g. Glycol,

Water etc., but in special circumstances the specification may be applied to onshore oil production and

petroleum product service, with the prior approval of the Owner.

1.1.3 Pumps for oil production and petroleum product services are covered by GES G.01, Centrifugal Pumps

(API 610), 8th Edition.

1.1.4 The Vendor/Contractor shall comply fully with the provisions laid down in the specification. Any

exception must be authorised in writing by the Owner.

1.1.5 In the event of any conflict between this specification and the Data Sheets, or with any of the applicable

Codes and Standards, the Vendor/Contractor shall inform the Owner in writing and receive written

clarification before proceeding with the work.

1.1.5 This General Engineering Specification will form part of the Purchase Order/Contract.

1.2 Other NOC Specifications

The following NOC Specifications are an integral part of this specification and any exceptions shall be

approved in advance by the Owner.

GES A.04 Noise Level Criteria and Noise Control of Mechanical Equipment

GES A.06 Site Data

GES G.01 Centrifugal Pumps (API 610)

GES K.10 General Purpose Steam Turbines (API 611)

GES L.11 Induction Motors (Low Voltage)

GES N.01 Thermal Insulation for Hot Service

GES S.06 Skid Assemblies

GES X.01 Surface Preparation and Painting Application

GES X.02 Colour Coding of Equipment and Piping Systems

GES X.03 External Protective Coatings

The Vendor/Contractor shall also ensure all Sub-Contractors comply with the relevant sections for the

above specifications.

1.3 Data Sheets

The technical data supplied by the Owner for the equipment is given on the ASME B73.1M and 2M Data

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Sheet which is included at the end of this specification. The Vendor/Contractor shall complete the Data

Sheet with the remaining information and return it with his bid.

Prior to shipment, the Vendor/Contractor shall submit a completed "As Built" Data Sheet.

2.0 DEFINITIONS

2.1 Technical

The technical terms used in this specification are as defined below:

NPSH Net positive suction head is the total suction head in feet of liquid absolute (at the pump

centreline or impeller eye) less the absolute vapour pressure in feet of the liquid being

pumped at the pumping temperature.

NPSHA NPSH available at the pump.

NPSHR NPSH required by the pump to prevent cavitation. Cavitation shall be deemed to have

taken place when the rated head has been reduced by 3% when the pump is operated at

rated flow.

Suction Specific Speed(S) S= rpm x _ gpm (NPSHR)0.75

2.2 Contractual

The commercial terms used in this specification are defined as follows:

Owner

The oil and gas company, an associate or subsidiary, who is the end user of the equipment and facilities.

Vendor

The company supplying the equipment and material.

Contractor

The main contractor for a defined piece of work

Sub-Contractor

A company awarded a contract by a contractor to do part of the work awarded to the Contractor.

Inspection Authority

The organisation representing the Owner or Contractor that verifies that the equipment and facilities have

been designed, constructed, inspected and tested in accordance with the requirements of this specification

and the Purchase Order/Contract.

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Inspector

A qualified individual representing the Owner, Vendor/Contractor or the assigned Inspection Authority,

who verifies that the equipment and facilities have been designed, constructed, inspected and tested in

accordance with the requirements of this specification and the Purchase Order/Contract.

3.0 DESIGN

3.1 Codes and Standards

3.1.1 Horizontal pumps shall conform to ASME B73.IM "Specification for Horizontal End Suction Centrifugal

Pumps for Chemical Process", as amended by this specification.

3.1.2 Vertical pumps shall conform to ASME B73.2M "Specification for Vertical In-Line Centrifugal Pumps for

Chemical Process", as amended by this specification.

Only where called for in this specification, both horizontal and vertical pumps shall comply with therequirements of API 610 "Centrifugal Pumps for Petroleum, Heavy Duty Chemical and Gas Industry

Services".

3.2 Additions and Exceptions to ASME B73.IM - Horizontal Pumps

Where paragraphs have been amended/deleted or new requirements added, these are identified.

ASME 4.1 Pressure and Temperature Limits

4.1.1 Add:

"The maximum discharge pressure shall apply to all parts of the pressure casing".

4.1.4 "Pumps with variable speed drivers shall be capable of operating continuously up to at

least 105% of rated speed, and shall be capable of operating briefly under emergency

conditions up to the trip speed".

ASME 4.2 Flanges

4.2.1 Add:

When cast iron pumps are specified, they shall have flat face flanges, all steel pumps

shall have raised face flanges.

ASME 4.3 Casing

4.3.1 Add:

"Drain connections shall be supplied at the lowest point of the pump casing".

4.3.5 Jackets shall not be used on the casing, nor the stuffing box.

4.3.7 Add new paragraph:

"A vent connection shall be supplied for the pump if the casing is not self-venting".

4.3.8 Add:

"For flammable or toxic liquids, connections shall be socket welded and terminate in a

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valve, and be gussetted."

ASME 4.4 Impeller

4.4.1 Add:

"Closed Impellers are preferred".

4.4.3 Delete the paragraph and replace by:

"All impellers shall be dynamically balanced to ISO Grade G.25 of ANSI S2.19".


Pumps with constant speed drivers shall have impeller sizes not exceeding 90% of the

maximum impeller size that can be installed in the pump casing. The head/capacity curve

shall rise continuously to shut off.

Pumps with constant speed drivers shall be capable of at least a 5% head increase at rated

conditions by replacement of the impeller with one of increased diameter".


"The NPSH requirement shall be based on water. NPSH correction factors for

hydrocarbon shall not be applied. At rated flow, NPSHR shall be at least 3.3 ft (1.0 m)

less than NPSHA or less than 0.66 x NPSHA whichever is the lower value. The

Vendor/Contractor shall also state in his proposal the NPSHR at 125% of rated capacity".


"Pumps that have stable head/capacity curves that continuously rise to shut-off are

preferred for all applications, and are required when parallel operation is specified. The

head rise shall preferably be 10-20% of the head at rated capacity".

ASME 4.5 Shaft

4.5.1 Add:

"All pumps shall be provided with a shaft sleeve sealed and locked to the shaft. The shaft

sleeve shall be resistant to wear, corrosion and erosion. The shaft sleeve shall be of the

replaceable type".

ASME 4.6 Shaft-sealing

4.6.1 Add:

"All pumps on process duty shall have mechanical seals. Welded metal bellows seals are

preferred.

All seals shall be single, balanced, hydraulic design, interior type.

Seals shall be identified by the classification in Appendix `D' of API 610, Eighth Edition.

The Vendor/Contractor shall provide seal piping and accessories as defined in Figures A2

and A3 of ASME B73.IM - 1991. Where the Owner has not specified the seal and piping plan on the Data Sheet, the Vendor/Contractor shall propose an arrangement suitable for

the duty for approval by the Owner.

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Seals shall be provided with a floating, carbon bushing, auxiliary sealing device".

4.6.2 In hot service (>212°F (100°C)) the seal fluid temperature shall not exceed 122°F (50°C);

the cooler shall be sized accordingly.

ASME 4.7 Bearings

4.7.1 Add:

"For pumps handling flammable or toxic liquids, the brackets between the pump casing

and the bearing housings shall be of steel".

4.7.5 Delete the first sentence, and replace by:

"Pump bearings and bearing housings shall be designed for oil lubrication".

ASME 4.8 Materials of Construction

4.8.1 Add:

"For flammable or toxic service, pump casings shall be in steel material".

ASME 4.12 Miscellaneous Design Features

4.12.1 Add:

"Coupling guards shall be easily removable and non-sparking".

4.12.7 "Baseplate and Rigidity"

Add the following paragraphs:

4.12.7.1 "All pumps shall be provided with a drip rim type baseplate. A tapped drain opening shall be

provided of not less than NPT 1 at the pump end of the baseplate.

Fabricated baseplates are preferred. The baseplate shall extend under the pump and

driver. Two screwed earthing bosses shall be welded to the baseplate, at diametrically

opposite corners.

4.12.7.2 Mounting pads shall be provided for the pump and driver. The pads shall be larger than the foot

of the mounted equipment to allow levelling of the baseplate without removal of the

equipment.

The pads shall be fully machined flat and parallel. Corresponding surfaces shall be in the

same plane within 0.002 inch per foot (0.17 mm per metre) of distance between the pads.

These requirements shall be met by suporting and clamping the baseplate at the

foundation bolt holes only.

4.12.7.3 All pads for drive train components shall be machined to allow for the installation of shims at least

_ ins (3 mm) thick under each component. A set of stainless steel shims at least _ ins (3

mm) thick shall be furnished".

Add new paragraph:

4.12.8 "Couplings

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Spacer type couplings shall be provided. The minimum service factor shall be 1.5, based

on the driver nameplate rating.

Couplings operating at or above 3500 rpm with shaft diameter over 2½ ins (65 mm) shall

be dynamically balanced and match marked".

Add new paragraph:

4.12.9 "Electric Motor Driver Power Selection

Electric motors shall comply with GES L.11.

Motors shall be sized with a nominal nameplate rating of at least the following minimum

percentage margin over the pump rated horse power:-

Table 1 - Motor Power Selection

Pump BHP Range % Margin Pump BHP Range % Margin

1-4 HP 30 51-75HP 15

5-25 HP 25 > 75 10

26-50 HP 20 -- --

Pump motors shall preferably be of sufficient size to operate the pump without overload

at the end of curve condition".

Add new paragraph:

4.12.10 "Piping

4.12.10.1 Steel pump casing connections and piping for vent and drain shall be welded and flanged,

and shall have the same rating as the pump discharge flange.

For cast iron pumps where use of a studded boss or flange is impractical, threaded

connections will be considered. Piping and fittings shall be socket or butt welded: seal

welded threaded joints are not acceptable. For non toxic non flammable service, socket

weld "unions" may be provided to allow disassembly and maintenance.

4.12.10.2 All piping, except cooling water piping, shall be Schedule 80 seamless pipe for sizes 1½

and smaller and Schedule 40 minimum for NPS 2 and over. Seal flush piping shall be

NPS ½ minimum Schedule 40S stainless steel pipe, socket welded.

4.12.10.3 Cooling water piping shall be NPS ¾ minimum, Schedule 80 seamless pipe or ½ ins

(12.7 mm) minimum stainless steel tubing, 0.035 ins (0.95 mm) minimum wall thickness.

4.12.10.4 Swage nipples or reducing couplings shall be used for pipe size changes. Bushings and

street elbows are not acceptable.

4.12.10.5 Casing drain and vent connections shall be valved as close as possible to the pump. The

piping shall extend to the edge of the baseplate.

4.12.10.6 There shall be sufficient space between the pump casing and baseplate to allow

installation and removal of the elbow and valve on the drain connection".

4.13 Add new paragraph:

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"Suction Specific Speed

Pumps shall have suction specific speeds (S) less than 11,000, in imperial units, (USgpm

and ft head) at the best efficiency point of the maximum impeller diameter."

ASME 5.1 General Information Application

5.1.3 Add:

GES A.04 shall apply. The sound pressure level measured at three feet (one meter) from

the surface of the pump and driver package shall not exceed 85 dB(A). The

Vendor/Contractor shall submit individual noise data for the pump and driver and the

combined noise spectrum for the pump and driver.

3.3 Additions and Exceptions to ASME B73.2M - Vertical Pumps

Where paragraphs have been amended/deleted, or new requirements added, these are identified from the

1991 Edition.

ASME 4.1 Pressure and Temperature Limits

4.1.1 Add:

"The maximum discharge pressure shall apply to all parts of the pressure casing".

4.1.4 "Pumps with variable speed drivers shall be capable of operating continuously up to at

least 105% of rated speed, and shall be capable of operating briefly, under emergency

conditions, up to trip speed".

ASME 4.2 Flanges

Add:

"When cast iron pumps are specified they shall have flat face flanges, all steel pumps

shall have raised face flanges".

ASME 4.3 Casing

4.3.1 Add:

"Drain connections shall be supplied at the lowest point of the pump casing".

4.3.5 Jackets shall not be used on the casing nor the stuffing box.

4.3.7 Add new paragraphs:

"A vent connection shall be supplied for the pump if the casing is not self-venting.

Where seal piping does not provide for natural seal face wetting during start-up, the

Vendor/Contractor shall provide seal vent piping and a valve".

4.3.8 "For flammable or toxic liquids, connections shall be socket welded, terminating in a

valve, and be gusseted".

ASME 4.4 Impeller

4.4.1 Add:

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"Closed impellers are preferred".

4.4.3 Delete the paragraph and replace by:

"All impellers shall be dynamically balanced to ISO Grade G.25 of ANSI/ASME S2.19".


"Pumps with constant speed drivers shall have impeller sizes not exceeding 90% of the

maximum impeller size that can be installed in the pump casing. The head/capacity curve

shall rise continuously to shut off".


"The NPSH requirement shall be based on water. NPSH correction factors for

hydrocarbon shall not be applied. At rated flow, NPSHR shall be at least 3.3 ft (1.0m)

less than NPSHA, or less than 0.66 x NPSHA whichever is the lower value. The

Vendor/Contractor shall also state in his proposal the NPSHR at 125% of rated capacity".


"Pumps that have stable head/capacity curves that continuously rise to shut-off are

preferred for all applications and are required when parallel operation is specified. The

head rise shall preferably be 10-20% of the head at rated capacity".

ASME 4.5 Shaft

4.5.1 Add:

"All pumps shall be provided with a shaft sleeve sealed and locked to the shaft. The shaftsleeve shall be resistant to wear, corrosion and erosion. The shaft sleeve shall be of the

replaceable type".

ASME 4.6 Shaft-sealing

4.6.1 Add:

"All pumps shall have mechanical seals. Welded metal bellow seals are preferred.

All seals shall be single, balanced hydraulic design, interior type.

Seals shall be identified by the classification in Appendix `D' of API 610, Eighth Edition.

The Vendor/Contractor shall provide seal piping and accessories as defined in Figures A2

and A3 of ASME B73.2M - 1991. Where the Owner has not specified the seal and

piping plan on the data sheet, the Vendor/Contractor shall propose an arrangement

suitable for the duty for approval by the Owner.

Seals shall be provided with a floating, carbon bushing, auxiliary sealing device".

ASME 4.7 Driver and Coupling Design

4.7.4 Motor Horsepower Selection

Delete the first sentence and replace by:

"All electric drive motors shall comply with GES L.11.

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Motors shall be sized with a nominal nameplate rating of at least the following minimum

percentage margin over the pump rated horsepower:-

Table 2 - Motor Power Selection

Pump BHP Range % Margin Pump BHP Range % Margin

1-4 HP 30 51-75HP 15

5-25 HP 25 > 75 10

26-50 HP 20 -- --

Pump motors shall be of sufficient size to operate the pump without overload, at the end

of curve condition."

4.7.6 Bearing - VB Pumps

Add new paragraph (d)

"Pump bearings shall preferably be designed for grease lubrication".

ASME 4.8 Materials of Construction

4.8.1 Add:

"For flammable or toxic service pump casings shall be in steel material".

ASME 4.12 Miscellaneous Design Features

4.12.1 Add:

"Coupling guards shall be easily removable and non-sparking".

Add new paragraph:

4.12.8 "Piping

4.12.8.1 Steel pump casing connections and piping for vent and drain shall be welded and flanged and have

the same rating as the pump discharge flange. For cast iron pumps where use of astudded boss or flange is impractical threaded connections will be considered. Piping and

fittings shall be socket or butt welded: seal welded threaded joints are not acceptable.

For non toxic non flammable service, socket weld "unions" may be provided to allow

disassembly and maintenance. Small bore auxiliary connections on seals may also be

screwed where space/access prohibit the use of flanges.

4.12.8.2 All piping, except cooling water piping, shall be Schedule 80 seamless pipe for sizes 1½ ins (38

mm) and smaller and Schedule 40 minimum for sizes 2 ins (50.8 mm) and over. Seal

flush piping shall be ½ ins minimum (12.7 mm) Schedule 40S stainless steel pipe, socket

welded.

4.12.8.3 Cooling water piping shall be ¾ in (19 mm) minimum, Schedule 80 seamless pipe or ½ ins (12.7mm) minimum stainless steel tubing, 0.035 ins (0.95 mm) minimum wall thickness.

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4.12.8.4 Swage nipples shall be used for pipe size changes. Bushings and street elbows are not acceptable.

4.12.8.5 Casing drain and vent connections shall be valved as close as possible to the pump".

Add new paragraph:

4.12.9 "Pedestals

The Owner shall specify if support pedestals are to be provided".

Add new paragraph:

4.12.10 "Couplings

The minimum coupling service factor shall be 1.5 based on the driver nameplate rating.

Couplings operating at or above 3500 rpm with shaft diameter over 2 ins (50 mm) shall

be dynamically balanced and match marked".

Add new paragraph:

ASME 4.13 "Suction Specific Speed

Pumps shall have suction specific speeds (S) less than 11,000, in imperial units, (USgpm

and ft head) at the best efficiency point of the maximum impeller diameter."

ASME 5.1 General Information Application

5.1.3 Add:

"GES A.04 shall apply. The sound pressure level measured at three feet (one meter) from

the surface of the pump and driver package shall not exceed 85 dB(A). The

Vendor/Contractor shall submit individual noise data for the pump and driver and the

combined noise spectrum for the package".

4.0 MATERIALS

4.1 ASME Requirements

4.1.1 Where materials are not specified, the Vendor/Contractor shall propose the most suitable materials for the

duty from paragraph 4.8 of ASME B73.1M - 1991 and ASME B73.2M - 1991, for the approval of the

Owner.

Similarly, in the absence of a detailed seal specification, the Vendor/Contractor shall also propose the most

appropriate mechanical seal type and materials using the API 610 designation, for the approval of the

Owner.

4.1.2 Materials, casting factors and the quality of any welding shall be equal to those required by Section VIII,

Division 1 of the ASME Code. The manufacturer's data report forms, as specified in the code, are not

required.

4.2 H2S Corrosion

4.2.1 Any corrosive agents present in the process fluids and in the environment, including constituents that may

cause stress corrosion cracking, will be specified by the Owner.

4.2.2 All materials subject to pressure and exposure to a medium (whether gas or liquid) containing H2S shall

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comply with the yield strength and hardness restrictions stipulated in NACE MR-01-75 (94).

When approved, wear surfaces may be hardened by the application of a suitable coating.

4.3 Miscellaneous

4.3.1 The use of chaplets in pressure castings shall be held to a minimum. The chaplets shall be clean and

corrosion free (plating permitted) and of a composition compatible with the casing.

4.3.2 Where mating parts such as studs and nuts of AISI Standard Type 300 stainless steel, or materials with

similar galling tendencies are used, they shall be lubricated with a suitable anti-seizure compound.

4.3.3 If austenitic stainless steel parts exposed to conditions that promote inter-granular corrosion are to be

fabricated, hard-faced, overlaid or repaired by welding, they shall be made of low carbon or stabilized

grades.

4.3.4 Minor parts that are not identified (such as nuts, springs, washers, gaskets and keys) shall have corrosion

resistance at least equal to that of specified parts in the same environment. Seal / O-ring material betweenthe shaft and the shaft sleeve shall be verified by the Vendor/Contractor as being satisfactory for the service

conditions.

Welding of piping, pressure-containing parts, and wetted parts, as well as any weld repairs to such parts,

shall be performed by personnel and procedures qualified in accordance with Section VIII, Division 1 and

Section IX of the ASME Code.

4.3.5 Impact testing is required for critical exposure temperatures below -20°F (-29°C).

4.3.6 PWHT is required for all carbon and ferritic alloy steel pressure containing components that are welded

and/or weld repaired, when the weldment is exposed to a process environment containing wet H2S. The

PWHT procedure outlined in the ASME Code, Section VIII, paragraphs UW-40, UW-49, UHA-32 andUCS-56 shall be followed, except that notes in Tables UHA-32 and USC-56 do not apply. All welds,

regardless of type or size, that are exposed to wet H2S shall be PWHT at a minimum temperature of 1100°F

(595°C). External attachments on P-1 Group 1 and 2 materials do not require PWHT.

4.3.7 Connections welded to pressure casings shall be installed as specified below.

Auxiliary piping welded to alloy steel casings shall be of a material with the same nominal properties as the

casing material or low-carbon austenitic stainless steel. Other materials compatible with the casing material

and intended service may be used with the Owner's approval.

Radiographic NDE of welds is preferred but where this is not possible, due to nozzle orientation, magnetic

particle or liquid penetrant inspection of welds will be required.

Repair welding shall not be carried out without the Owner's approval including approval of the weld

procedures to be used.

4.3.8 Asbestos shall not be used in any form which can result in free asbestos becoming a health hazard. The

Vendor/Contractor shall declare all asbestos use and submit alternative material for review by the Owner.

4.4 Mechanical Seals

Springs shall be Alloy 20 or 316 stainless steel. Other metal parts shall be 316 stainless steel or another

corrosion-resistant material suitable for the service, except that metal bellows shall be of the seal

manufacturer's recommended material for the service. Metal bellows shall have a corrosion rate of less

than 2 mils (51 micrometres) per year.

Mechanical seal gasket materials shall comply with the table below:

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Table 3 - Temperature Limits on Mechanical Seal Gaskets

Gasket Material

Ambient or Pumping Temperature F (

C)

Minimum Maximum

TFE -20 (-29) +350 (+177)

Nitrile (Buna-N) -20 (-29) + 210 (+99)

Neoprene 0 (-18) +200 (+93)

Fluoroelastomer 0 (-18) +350 (+177)

FFMK Elastomer + 10 (-12) +350 (+177)

Graphite Foil -20 (-29) +350 (+177)

5.0 INSPECTION

5.1 Procedures

5.1.1 The inspection requirements are covered by the document "General Conditions of Purchase" which forms

part of the Purchase Order/Contract. Additional requirements are given below.

5.1.2 All items of plant and equipment referenced within this specification shall be subject to inspection by the

Owner or the Inspection Authority.

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5.1.3 Inspection shall be in accordance with 4.1 and 4.2 of API 610 Eighth Edition as amended by this

specification. All inspection activities to be performed, including any special requirements, shall be agreed

with the Owner and shall be incorporated within the agreed Quality Control Plan provided by the

Vendor/Contractor. The Vendor/Contractor shall submit procedures for all applicable NDT techniques for

approval by the Owner before production commences.

5.1.4 All operators of NDT equipment shall have thorough knowledge of the operation of the equipment to be

used and shall hold an appropriate certificate of competence, which is to be agreed by the Owner.

5.1.5 The Vendor/Contractor is to furnish the Owner's Inspector with all reasonable facilities, to satisfy himself

that the equipment is fabricated and tested in accordance with the relevant code and this specification.

5.1.6 Any approvals given by the Owner's Inspector and/or the Inspection Authority do not relieve the

Vendor/Contractor of any responsibility regarding guarantees, workmanship or compliance with the code

and this specification.

5.2 Scope

Inspection and testing shall comply with paragraphs 4.1 and 4.2 of API 610, as amended below:

API 4.1 General

4.1.4* The Owner reserves the right to observe any inspection carried out by the Vendor/Contractor, as

agreed at an inspection coordination meeting to be held within four (4) weeks of order placement.

4.1.6* Appendix "N" (Inspector's checklist) is not applicable.

API 4.2 Inspection

4.2.1.3 Delete and replace with:

"The Vendor/Contractor's Quality Control Plan shall be submitted with his proposal and shall

specify the parts to be examined and the type of examination the Vendor/Contractor intends to

carry out. The proposed quality plan is subject to the approval of the Owner."

4.2.3.1* A cleanliness inspection is not required.

4.2.3.2* Hardness verification is only required if hydrogen sulphide is present (paragraph 2.11.1.11 of API

610).

5.3 Nameplates

Nameplates shall be provided complying with paragraph 3.6 of API 674.

6.0 TESTING

6.1 Required Tests

The following tests may be required and witnessed by the Owner:

- hydrostatic (mandatory)

- mechanical run (mandatory)

- performance (if specified)

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- NPSHR (if specified)

- Auxiliary equipment (if specified)

- Vibration (if specified)

The Owner may waive the execution and/or witnessing of the tests if the pumps involved are of small

power requirements or where NPSHA significantly exceeds NPSHR. Specific requirements will be given

on the Data Sheet by the Owner.

6.2 Test Requirements

6.2.1 Test requirements as indicated on the Data Sheet shall be carried out in accordance with paragraphs (a) to

(f) below:

(a) Hydrostatic Test

A hydrostatic test complying with paragraph 5.2.1 of ASME B73.1M - 1991/ASME B73.2M - 1991 asamended below, shall be carried out on pressure containing components of all pumps except:

5.2.1 - Delete "10 minutes" and replace with "30 minutes".

(b) Mechanical Run

The mechanical run shall be at rated head and speed for a minimum period of one (1) hour.

(c) Performance Test

Paragraph 5.2.2 of ASME B73.1M - 1991/ASME B73.2M - 1991 shall apply. Performance curves

shall comply with paragraph 5.2.3 of ASME B73.1M - 1991 and ASME B73.2M - 1991, and shall beincluded in the data book.

(d) NPSHR Test

NPSHR tests, when required, shall comply with paragraph 4.3.4.1 of API 610 8th edition. Testing shall

be carried out with contract mechanical seals installed.

(e) Auxiliary Equipment Tests

When required auxiliary equipment such as oil systems, gears and control systems shall be tested in the

Vendor's/Contractor's shop. Details of the auxiliary-equipment test shall be developed jointly by the

Owner and the Vendor/Contractor.

(f) Vibration Test

Vibration readings, when required, shall be taken on the bearing housings. Unless otherwise agreed,

the acceptance limits shall be as stated in API 610 paragraphs 2.8.3.7 to 2.8.3.9.

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6.2.2 For all specified tests above the Vendor/Contractor shall submit test procedures in writing to the Owner for

approval prior to the start of the testing programme. The test procedures shall be detailed and include the

acceptance criterion (for each test) which shall be internationally accepted.

6.2.3 No preservative or paint shall be applied to welds, mechanical joints or pressure containing components

prior to any hydrostatic test.

6.2.4 All test gauges shall have been calibrated within 12 months and the calibration certificates made available

to the Inspector.

6.3 Test Certificates

Test certificates shall be provided as follows:-

(a) The manufacturer's physical and chemical certification for pressure containing parts

(b) NDT certification (radiographic, magparticle, ultrasonic, dye penetrant)

(c) Hydrotest certificates

(d) Shop mechanical run/performance/NPSH test data

7.0 DOCUMENTATION

7.1 Introduction

7.1.1 This section covers the documentation requirements for design, materials, inspection, testing, installation

and operation of the pump(s).

7.2 Schedules and Reports

7.2.1 The Vendor/Contractor shall supply with his proposal, a schedule showing submission of all documents for

review and approval, proposed Sub-Contractors and material procurement and a production/fabrication

programme.

7.2.2 The Vendor/Contractor shall submit with his proposal a Quality Control Plan for the contract.

7.2.3 After the contract award, monthly reports on design, material procurement and production progress shall be

submitted to the Owner.

7.2.4 A co-ordination meeting shall be held within six (6) weeks of the placement of the Purchase

Order/Contract, to review all engineering and manufacturing requirements of the order.

7.3 Data and Drawings

7.3.1 The documents detailed below shall be submitted for approval/review to the Owner and to the Inspection

Authority within the periods agreed between the Owner and Vendor/Contractor. It shall be the

responsibility of the Vendor/Contractor to ensure that the production schedule takes into account

documentation submission periods, plus a three (3) week approval review period by the Owner and/or the

Inspection Authority. The Vendor/Contractor shall be responsible for obtaining approvals from the

Inspection Authority.

7.3.2 All calculations shall be carried out in a clear and logical manner. The source of formulae or methods shall be clearly referenced. Computer calculations will only be accepted if all input is shown, together with

calculated values of intermediate terms and factors and the computer program has been validated to the

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satisfaction of the Owner.

7.3.3 The Vendor/Contractor shall submit as a minimum, the data and drawings listed below:

For Proposals (Typical Data)

(a) Performance curves

(b) Outline drawing with max forces on nozzles

(c) Data sheet completed

(d) Seal description and piping arrangement

(e) Cross section drawings

For Contract (Certified Data)

All document items listed in Appendix "A" of ASME B73.1M and B73.2M 1991 with the addition of the

following:

(a) General arrangement of motor with cable box details

(b) Coupling drawing

(c) Appendix "A" Parts list paragraph A3.3(b) refer to paragraph 8.2 of this specification for operating

spares period.

7.4 Manuals

Requirements for data books and Installation Operation and Maintenance Manuals are as follows:

7.4.1 Data Books

Two (2) copies of the data book shall be provided containing the shop manufacturing Record/Test

Certificates.

7.4.2 Installation, Operating and Maintenance Manuals

Six (6) copies of Installation, Operating and Maintenance Manuals shall be provided containing the

information defined in Appendix "A" of ASME B73.1M and B73.2M 1991 and the data and drawings

referred to in section 7.3.3 of this specification.

8.0 PRIOR TO SHIPMENT

8.1 Painting and Coatings

Surface preparation and painting shall be in accordance with GES X.01, GES X.02 and GES X.03. The

Vendor/Contractor may offer their own paint system, suitable for the duty, as an option.

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8.2 Spares

The Vendor/Contractor shall submit with his initial equipment proposal, a priced list of recommended spare

parts for "Start-up" and for "Two Years Operation".

8.3 Packing and Storage

This section describes the minimum requirement for the preservation and protection of reciprocating pumps

during the sea and land transportation and storage, prior to installation.

Additions and Exceptions to API 610

The preparation for shipment shall comply with API 610 Section 4.4 as amended below:

4.4.1* Delete this paragraph and replace with:

The equipment shall be prepared for export shipment by sea. Shipment as non-containerised

deck cargo is not permissible.

The probable storage period will be specified in the order/enquiry and will extend from the

time of despatch to the time of unpacking at site. If the storage period is not stated, a

minimum period of twenty-four (24) months shall be assumed.

4.4.3.2 Delete the first sentence and add:

The Vendor/Contractor shall request and obtain the Owner's authorisation if he recommends

disassembly of any pump for shipment.

4.4.3.3 Delete this paragraph and replace by:

Painting shall comply with GES X.01, GES X.02 and GES X.03, unless manufacturer's

standard paint system has been approved by the Owner.

4.4.3.13 Add the following paragraph:

Mechanical seals, carbon rings and other sealing devices shall be installed for shipment. If

shaft packing is required, two sets of packing in unused condition shall be supplied, one set

installed and one set boxed and shipped attached to the equipment.

8.4 Shipping

Detailed shipping arrangements are covered by the Purchase Order/Contract.

The equipment shall not leave the Vendor's/Contractor's works for shipment until the release has been

approved by the Owner's Inspector.

8.5 Warranty

The Contractor shall provide manufacturer's written guarantees of the pumps performance. Curves of head

versus flow with efficiency and power lines shall be provided to cover the operating range.

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The Vendor/Contractor shall warrant all materials and services supplied against any defect for a minimum

of twelve (12) months after commissioning or twenty-four (24) months from the date of delivery to site,

whichever is the shorter period, or for the period stipulated in the Order.

Should any item be found defective, the Vendor/Contractor shall be responsible for all costs associated

with restoring the equipment to the standard specified by the Purchase Order/Contract.

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CLIENT

PLANT SHEET 1 of 1

SERVICE ITEM No. No. of UNITS

ASME B73.1M-1991 ASME B73.2M-1991

1 Vendor /Contractor

2 Pump Size and Model BRG. Frame Service

4

5 Liquid/Slurry Performance Curve No.

6 PT.°F Norm Max. US GPM at Norm Rated RPM NPSH (Water)

7 SP.GR. At Norm PT Total Head, FT Rated Eff. % BHP Rated

8 VAP, Press. At Norm PT. PSIA Suct. Press. PSIG Max. Rated Max. BHP Rated Impeller

9 Vis. At Norm PT SSU NPSHA, FT Max. Head Rated

10 Corr./Eros. Caused By PH HYD. HP Max. Disch. Press. PSIG

11 Driver HP to be Selected for Max. S.G. & Max. Viscosity Min. Continuous GPM

12

13 CONSTRUCTION ASME B73.1M ASME B73.2M OTHER

14 Pump Type: Horiz. Vert.In-Line Coupled Motor Shaft Nonwit. Perf. Wit. Perf.

15 Cradled Mnt. Nonwit. Hydro. Wit. Hydro.16 Case Horizontal Mount: Foot Centerline Nonwit.NPSH Wit. NPSH

17 Verticle Mount: Motor Shaft Rigid Coupling Other Nonwit. Vibration Wit. Vibr.

18 Split: Radial Axial Type Volute: Single Double Dismantle & Inspect after Test

19 Press: Max.Allow. PSIG °F Hydro Test PSIG Other

20 Connect: Drain Gage Suction Gage Discharge

21 Impeller Dia. Rated Max. Impeller Type

22 Bearings Type: Radial Thrust

23 Lube: Oil Oil Mist Grease Grease for Life Casing

24 Coupling: MFR Model Guard Oiler Impeller

25 Driver Half MTD. By: Pump MFR. Driver MFR. Purchaser Wear Rings

26 Stuffing Box Cover: Standard Jacketed Seal Only Shaft/Sleeve

27 Packing: MFR. & Type Size/No. of Rings Gland

28 Lantern Rings: Yes No Gaskets

29 Mech. Seal: MFR. & Type Material Code Baseplate

30 Balanced Unbalanced Single Inside Outside Coupling Guard

31 Double Back to Back Tandem Face to Face Other:

32 Cartridge

33

34 Stuf. Box Plan No. C.W. Piping Plan No. INSPECTION Not Required

35 Total Cooling Water Req'd. GPM Sight F.I. Req'd. In Process Final

36 Packing Cooling Injection Req'd. Total GPM PSIG Days Notification Required

37 External Seal Flush Fluid GPM PISG

38 Seal Quench Plan Seal Quench Fluid

39 DRIVER: Motor Turbine Other Provided By

40 HP RPM Frame Volts/Phase/Hertz

41 MFR. Bearings Service Factor

42 Type Insulation AMPS: FL LR

43 Lube Temp. Rise °F Encl.

44 Inlet Press. Exhaust Press. Steam Temp. Water Rate

45 Other

46 Customer/User

47 Location

48 Customer P.O. No.

49 Item No(s) Equip. No(s)

50 Factory Order No(s) Pump Serial No(s)

Revision No./Date

Prepared by/Date

Authorised by/DatePurpose

(C) 1999 NATIONAL OIL CORPORATION. The information on this sheet may be used only for the purpose for which it is supplied by NOC.

3 No. Pumps Req'd No. Motors Req'd Item No.

AUXILIARY PIPING (See Figs. A2 and A3 For Code)

DATA SHEET No.

P.O. / CONTRACT No.

CENTRIFUGAL PUMP DATA SHEET FORM A1

OPERATING CONDITIONS - EACH PUMP PERFORMANCE

No. Turbines Req'd Item No.

ADDITIONAL REQUIREMENTS/COMMENTS

PUMP MATERIAL

SOUND SPECIFICATION REQUIREMENTS

SHOP TESTS

Documents

G-02 NOC