Pig Launcher and Receiver Specification Rev 3

The Shell Petroleum Development Company of Nigeria Limited

Pipeline System

Pipeline West Re Entry Repair Project

Pig Launcher & Receiver Specification

SPDC- PP- 2007-02-00000244

Version: 3

February, 2007

Pig Launcher and Receiver Specification

Title:

Pig launcher and receiver specification

Author:

Wilson Andrew - EPG-PN-PPII

Reviewed by:

Kamal Jangra - EPG-PN-PPM

Approved by:

Dave Abbs - EPG-PN-TEFD

Document Owner:

EPG-PN-PP

Process Name:

Establish work specific Standards and Procedures

EPBM Code:

ACT.01.06.01

Document Number:

SPDC-2007-02-00000244

Issue Date:

February, 2007

Version:

R3

Retention Date:

November 2011

Review Date

November 2008

Confidentiality:

Un-classified R2 Section 3.0 Change title of DEP to design of pipeline pig trap R2 Section 4.5 Remove reference to PII R2 Section 14.1 to 14.12 Data sheets remove reference to Clamp on pig signallers R2 Section 14.4 & 14.11 Data sheets change pig barrel size from 22” to 24” R2 Section 14 Change Data Sheet 8,9,10, 17& 18 A / B to Major Barrel 4100mm & Minor Barrel 1500mm

Change History:

R2 Section 14 Change Data Sheet 12, 17& 18 A / B to Major Barrel 5100mm and Minor Barrel 1500mm R2 Section 14 Change Data Sheet Design Operating pressure to 1087.8 – psi for 16” and 20” R2 Page 38 Data sheet SPDC-2007-02-00000244 R2 Page 22 Data sheet

/ 13 Odidi 1 F/S 8’’ Launcher

SPDC-2007-02-00000244 / 12 Egwa 1 F/S 8’’ Launcher

R3 Change N4 Pig signaler to 4’’ from 2’’ To be modified for use as a balance line. Change Drain line to 4’’ from 6’’ Page 17 and 23 of 42 (20’’ Receiver and launcher) Change N4 Pig signaler to 4’’ from 2’’ To be modified for use as a balance line Page 25 (16’’ Receiver) ALL 8’’ Traps Kicker line to 4’’ from 6’’ and drain lines to 4’’ from 2’’

Version

Date

Pages

Draft

28 Feb, 2007

1

16 Mar, 2007

ALL

2

14 Mar,2007

22 and 38

3

07 May,2007

17,23 and 25

ALL

Remarks Initial issue for review and comment Approval and distribution Addition of 2 Pig Trap Data sheets Incorporation of Balance Line on 20’’ Receiver and Launcher and 16’’ Receiver Change. of Nozzle dimensions

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February, 2007

Pig Launcher and Receiver Specification ELECTRONIC SIGNATURE APPROVAL

LIST OF COPY HOLDERS Copy No. 01 02 03

Copy Holder Master Copy (DCC) Pipeline West Re-Entry Project PN-PPII (Pipeline West Asset Holder)

SPDC- PP- 2007-02-00000244

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No. of Copies 1 1 1

February, 2007


TABLE OF CONTENTS

1.0 2.0 3.0 4.0 4.1 4.2 4.3 4.4 4.5 4.6 4.7 4.8 4.9 4.10 4.11 5.0 6.0 7.0 8.0 9.0 10.0 11.0 12.0 12.1 12.2 13.0 14.0 14.1 14.2 14.3 14.4 14.5 14.6 14.7 14.8 14.9 14.10 14.11 14.12 14.13

Introduction..................................................................................................................................................... 5 Scope............................................................................................................................................................... 5 Terms of reference .......................................................................................................................................... 6 DESIGN REQUIREMENTS .......................................................................................................................... 7 Pressure Containing Parts ............................................................................................................................... 7 General............................................................................................................................................................ 7 Design Calculations Design Calculations ....................................................................................................... 7 Barrel .............................................................................................................................................................. 7 Length of Trap ................................................................................................................................................ 8 Barrel Connections ......................................................................................................................................... 8 Pig and Sphere Passage................................................................................................................................... 8 Pig and Sphere Handling ................................................................................................................................ 8 Barrel Reducer and Pipeline Pup .................................................................................................................... 8 Pig Signaller ............................................................................................................................................... 9 End Closure................................................................................................................................................ 9 Material........................................................................................................................................................... 9 Fabrication .................................................................................................................................................... 10 Shop Inspection and Testing ......................................................................................................................... 10 Quality Assurance......................................................................................................................................... 10 Tagging and Identification ............................................................................................................................ 10 Painting and External protection................................................................................................................... 11 Documentation.............................................................................................................................................. 11 PACKING AND SHIPPING ........................................................................................................................ 11 General Packing Requirements ................................................................................................................ 12 General Preservation Requirements ......................................................................................................... 12 Deliverable Schedule .................................................................................................................................... 14 ATTACHMENTS – FACILITY DATA SHEETS ....................................................................................... 15 1x 20’’ Receiver at Keremo M/F ............................................................................................................. 15 1x 8’’ Receiver for 8” Delivery line from Odidi 1 F/S ............................................................................ 15 1x 8” Launcher at Odidi 1 F/S ................................................................................................................. 15 1x 20’’ Launcher at Egwa 2/Odidi2 Pigging M/F to Keremo M/F .......................................................... 15 1x 16’’ Receiver at Egwa2/Odidi2 MF for 16” trunk line from Jones Creek .......................................... 15 1x 8’’ Receiver at Egwa2/Odidi2 M/F for 8” delivery line from Egwa2 F/S .......................................... 15 1x 8’’ Launcher at Egwa 2 F/S................................................................................................................. 15 1x 8’’ Receiver at Egwa2/Odidi2 MF for 8” delivery line from Odidi 2 F/S........................................... 15 1x 8’’ Launcher at Odidi 2 F/S................................................................................................................. 15 1x 8’’ Receiver at Egwa 1 MF for 8” delivery line from Egwa 1 F/S...................................................... 15 1x 8’’ Launcher at Egwa 1 F/S................................................................................................................. 15 1x 8’’ Launcher at Batan F/S ................................................................................................................... 15 1x 8’’ Receiver at Batan M/F for 8” Delivery line from Batan FS .......................................................... 15

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February, 2007

Pig Launcher and Receiver Specification 1.0

Introduction Various pipeline manifolds have been subject to third party damage in the western operating areas, as a result number of pig launcher/receivers need to be replaced. For full details of required traps see project pig trap data sheets which shall form part of the procurement package.

2.0

Scope This Specification defines the minimum requirements for the design, materials, manufacture, testing and inspection for pipeline pig launchers and receivers (pig traps) in stabilised non-sour crude oil service for ANSI Class ratings between ANSI 150 and ANSI 600. Pig traps manufactured to the requirements of this specification shall be used for launching and receiving pigs for bi-directional operational pipeline cleaning, de-waxing and batching activities and for the unidirectional launching and receiving of intelligence gathering on line inspection tools. The pig traps are intended for horizontal installation. Schedule of Requirements; 1) 2) 3) 4) 5) 6) 7) 8) 9) 10) 11) 12) 13)

1 x 20” Receiver at Keremo M/F 1 x 8’’ Receiver for 8” Delivery line from Odidi 1 F/S 1 x 8” Launcher at Odidi 1 F/S 1 x 20’’ Launcher at Egwa2/Odidi 2 Pigging M/F to Keremo M/F 1 x 16’’ Receiver at Egwa2/Odidi2 MF for trunk line from Jones Creek F/S 1 x 8’’ Receiver at Egwa 2/Odidi2 M/F for 8” Delivery line from Egwa2 F/S 1 x 8” Launcher at Egwa2 F/S 1 x 8’’ Receiver for 8” Delivery line from Odidi 2 F/S 1 x 8’’ Launcher at Odidi 2 F/S 1 x 8’’ Receiver for 8” Delivery line from Egwa 1 F/S 1 x 8’’ Launcher at Egwa 1 F/S 1 x 8” Launcher at Batan F/S 1 x 8’’ Receiver at Batan for 8” Delivery line from Batan FS

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February, 2007


Terms of reference Unless otherwise specified the latest editions of the documents, including all addenda and revisions, shall apply. This specification makes reference to the following documents:

International Standards American Standards ANSI B16.5 ANSI B16.9

Pipe Flanges and Flange Fittings Factory made Wrought Steel Butt welding Fittings

ANSI B31.4

Pipeline transportation systems for liquid hydrocarbons and other liquids

API 1104

Standard for welding pipelines and related facilities

ASTM D695

Test for comprehensive properties of rigid plastics

ASME V ASME VIII, Div. 1

Non-destructive examination techniques Unfired Pressure Vessels

ASME IX

Qualification standard for welding and brazing procedures, welders and brazers and welding and brazing operations Steel Pipeline Flanges Specification for Structural Steel Alloy Steel Bolting for High Temperature Service. Carbon and Alloy Steel Nuts for High Temperature Service. Non-Destructive Testing of Steel Forgings:

MSS-SP 44 ASTM A 36 ASTM A 193 ASTM A 194 ASTM A 275

British Standards BS 2633

Specification for Class 1 arc welding of ferritic steel pipe work for carrying fluids

BS EN 1435

Non-destructive testing of welds Radiographic testing of welded joints

BS EN 10029

Specification for tolerances on dimensions, shape and mass for hot rolled steel plates 3 mm thick or above

BS 4518

Specification for metric dimensions of toroidal sealing rings ('O'-rings) and their housings

BS EN 13445

Specification for unfired fusion welded pressure vessels

BS 5996

Methods for ultrasonic testing and specifying quality grades of ferritic steel plate

BS 7079

Preparation of steel substrates before application of paints and related products

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February, 2007

Pig Launcher and Receiver Specification SPDC Design Engineering Practices DEP 31.40.10.13 Gen

Design of pipeline pig trap systems

DEP 31.22.20.31 Gen

Technical specification for Pressure vessel amendments and supplements to ASME VIII division1 and division 2

DEP 31.40.21.30 Gen

Technical specification for pipeline fittings amendments/supplements to MSS SP-75

DEP 31.40.20.30 Gen

Technical specification for line pipe use in Oil and Gas operations under non-sour conditions Amendments/supplements to API Spec 5L

DEP 30.48.00.31 Gen

Technical specification for painting and coating of new equipment

4.0

DESIGN REQUIREMENTS

4.1

Pressure Containing Parts All those parts subjected to service pressure. In addition to these parts, studs, nuts, bolts and gaskets connecting pressure-containing components shall also be deemed to be pressure-containing parts

4.2

General The pig trap barrels and all branch connections shall be designed, constructed, inspected, tested and certified in accordance with ANSI B31.4. All piping, fittings, valves, etc., shall be designed to withstand the design pressure at the selected design temperatures. The flange and valve class shall be selected so that the pressure rating per ANSI B16.5 meets or exceeds the design pressure of the pipeline system at the scraper trap location. The pig traps shall be furnished with quick opening end closure for the insertion and removal of pigging equipment. Such end closures shall be design, constructed, inspected tested and certified in accordance with the requirements of ASME VIII.

4.3

Design Calculations Design Calculations All calculations for all launcher/receiver components shall be submitted to the Client for approval.

4.4

Barrel Length shall be to facilitate insertion of pigs into the barrel; the internal diameter shall be larger than the internal diameter of the pipeline. The diameter of horizontal barrels shall be:a)

For pipelines smaller than 20-inch diameter, the diameter of the major barrel should be 2 inches greater than the pipeline diameter.

b) For Pipelines with a diameter of 20-inch or greater the oversize should be 4 inches. Cylindrical sections shall be made from seamless or longitudinal seam welded pipe or from rolled and seam welded plate. Spiral weld seams in the barrel are prohibited. Reference shall be made to company standard - DEP 31.40.10.13 Gen.

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February, 2007


4.5

Length of Trap All pig traps are intended to accommodate online inspection intelligence gathering pigs (“intelligent” or “smart” pig) capable of negotiating two back-to-back bends of minimum radius of 5 pipeline diameters. The barrel length provided on the data sheets are Extracted from DEP 31.40.10.13 Gen. Table 3

4.6

Barrel Connections All barrel nozzles shall be minimum 50 NS (2") and flanged. Flanges to be in accordance with ANSI B16.5 and MSS SP- 44 as applicable. Outlets 75 NS (3") and larger shall be internally contoured. Guide bars shall be fitted to 100 NS (4") and larger outlets. Branch connections shall be welded, forged or extruded. All necessary reinforcements of locations such as openings, supports etc. shall where possible, be provided by self compensating nozzles and/or increased shell thickness. A detailed stress analysis may be required to ensure that the applied loadings and consequent stress is within code requirements. The use of reinforcing plates at vessel nozzles and doubling plates at vessel supports and attachments shall be minimized and will only be acceptable if approved by the Client. Where approved, reinforcing plates shall conform to the specified codes/standards and be fully welded. Vent holes shall be provided, tapped 1/8" NPT and plugged with a high melting point grease not capable of retaining pressure.

4.7

Pig and Sphere Passage Internal diameter of the minor barrel shall match that of the pipeline to which the pig trap is installed and wall thickness variations shall be accommodated by changes in the outside diameter to allow free passage of pigs and spheres. Similarly, the major barrel internal diameter shall be uniform with wall thickness variations being accommodated by changes in the outside diameter.

4.8

Pig and Sphere Handling A pig/sphere-handling device is required. The manufacturer shall provide a design of a device that allows pigs to be offered and inserted in to the trap or removed from the trap without the need for lifting of the pig or for personnel to place their head or upper body in to the trap. Lugs shall be provided on the launcher/receiver barrel either side of or adjacent to the enclosure. The lugs shall be the in the horizontal plane and suitable, for attaching a 50mm shackle.

4.9

Barrel Reducer and Pipeline Pup The pig trap barrel reducer shall be eccentric with the bottom flat. Designs utilizing concentric reducers shall not be used. The reducing section length of the eccentric reducer shall be at least as long as the internal diameter of the major barrel. The minor barrel shall have an inside diameter matching that of the pipeline specified in the attached data sheet.

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February, 2007


4.10

Pig Signaller Pig signalers shall be installed on both sides of the pig trap valve. The purpose of these signalers is to provide confirmation that the pig has been successfully launched and has successfully passed through the pig trap valve. For launcher the signaler on the downstream side of the pig trap valve would be located on the pipeline at a distance from the main tee of at least the length of the maximum length pig to be used. Pig signalers shall be the non-intrusive type. Proprietary signalers designed for removal under pressure normally have small-size flange and bolt assemblies and consideration should be given to the use of a standard 50 mm (2 inch) flange assembly for such items.

4.11

End Closure The barrel end closure shall be a quick opening closure. All moving parts of the closures should have lubrication facilities. The end closure shall be designed to comply with ASME VIII Div.l section UG-35 (B) (Quick actuating Closures) and DEP 31 22 20 31 GEN and the design, material selection and fabrication of the end closure doors shall be in accordance with DEP 31.40.21.30 Gen The end closure shall consist of the following components:a)

A removable door, which provides full-bore access when open, and terminates and seals the bore when closed

b) A welded end hub, for joining to the major barrel of a pig trap. The material used for the welding end hub shall be compatible with the barrel material as provided in the data sheet c)

A Closure handling device suitable to lift, hinge or swing the door, when the handling device is attached to the closure. it shall be attached to the welded hub not the major barrel of the pig trap

d) Two safety devices to prevent inadvertent opening of the closure before the pig trap is de pressurised.

5.0

e)

The closure door shall be installed in the vertical plane with the hinge located on the horizontal axis of the door to eliminate the need for any lifting or partial lifting of the door to open or close and allow the door to naturally remain in any open or partial open position.

f)

All required tools and actuators shall be provided and suitable attachment lugs for the tools shall be incorporated where necessary.

Material All materials in contact with line fluids shall comply with the requirements of ANSI B31.4 / API 5L, including all applicable Design Engineering Practices (DEP) addendums listed in section 3.0. Material Product Specification Level (PSL) shall be PSL2 to meet the requirements of API5L. Unless unavoidable, the resultant mechanical properties of the materials used in the construction of the pig hatch shall be similar to API 5L Grade X 52 and variations shall be subject to approval by the client technical authority.

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February, 2007


Fabrication All fabrication welds shall be in accordance with ASME Section VIII, Div. 1 Pressure Vessels, including all applicable Design Engineering Practices addendums listed in section 3.0 Wall thickness at welded joints shall match. Flange bolt holes shall straddle centre line of scraper trap. Permanent marking as necessary for material identification shall be by round nose or low stress stamps. Heat treatment shall be in accordance with the requirements of ASME Section VIII, Div. 1. Stress relieving of welds with respect to thickness for piping components shall be in accordance with ASME Section VIII, Div. 1.

7.0

Shop Inspection and Testing All welds and contoured nozzles shall be 100% NDT – full procedures are to be provided for review and approval by the client. Hydro test shall be in accordance with ASME Section VIII Div. 1 for a minimum period of l hour and in accordance with the requirements of standards listed in section 3.0 Client reserves the right of access at any time during fabrication and inspection/testing

8.0

Quality Assurance Contractor shall have in place an effective quality assurance system is in operation for both products and services and this shall comply with ISO 9001 or equivalent as approved by the Client. Contractor shall provide full inspection and test plan and shall comply with their Quality Assurance procedures as submitted and approved by the Client and if necessary, only modified if agreed to by the Client in writing.

9.0

Tagging and Identification A corrosion resistant name plate shall be permanently affixed to each equipment item supplied and shall bear, as applicable, the following data: a)

Name of Manufacturer

b)

Date of Manufacture

c)

Manufacturer Serial Number

d)

Trap nominal size (pipeline diameter)

e)

Design Code

f)

Pressure Rating, barg

g)

Design temperature range °C

h)

Design Pressure °C

i)

Hydrostatic Test Pressure, barg

j)

Clients PO Number

k)

Body Material

l)

End Closure Material

m)

Weight of Unit

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February, 2007


Painting and External protection Complete units shall be painted in accordance with DEP 30.48.00.31 Gen Contractor is required to provide adequate external protection against corrosion from salt laden atmosphere in summer and winter for all exposed surfaces. This applies to the barrels, closure door, seals and to all appurtenances. All openings shall be protected for shipment

11.0

Documentation Documentation shall be as listed below, and shall include as a minimum but not limited to the following certificates of all source materials, calculations, non-destructive examination (NDE) MT,PT,UT,RT,VTand hydro test results. and applicable records in support of verification The following documentation shall be provided to the schedule shown for each of the Pig launcher receivers supplied to the client: These records shall include the following: a) Details of heat treatment. b) Details of chemical analysis and mechanical test results. c) Sketches indicating the position and extent of any major weld rectification. d) Weld procedures and welder qualification to fully comply with the stated standards shall be made available e) Records relating to Non Destructive testing and visual Inspection f) Manufacturing and welding procedures. g) Material certs h) Calculations according to the relevant codes for the body and neck including extruded branch connections and quick opening end closure. i)

Trap assembly and sectional drawings showing all parts and accessories with materials and dimensions

j)

General arrangement and detailed drawings of pig handling system.

k) Quality Control Manual and Quality Control Plan; Manufacturing of the Pig traps shall commence only after approval of the above documents. Once the Company has approved the above-mentioned documents, any changes in design, material and method of manufacture shall be notified to the Company, whose approval in writing of all changes shall be obtained before the pig Launcher are manufactured. After approval, Contractor shall submit to Company all the approved drawings, documents and specifications.

12.0

PACKING AND SHIPPING Preparation for packing and shipping shall be in accordance with the attachments to the Material Requisition. Contractor shall be responsible for ensuring that the packing, marking instructions, shipment and storage of the equipment is in accordance with the following requirements:

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February, 2007


General Packing Requirements a)

The Contractor is responsible in determining the necessary preparation, need for the conditions as described on the attached environmental data sheet.

b) Contractor’s quotation shall include a description of the preparation offered. All costs to provide preparation shall be included. c)

All tags and marking on equipment, crates, and packages shall be fade resistance, withstanding extended periods of storage in bright sunlight and other atmospheric conditions prevalent at the job site.

d) Equipment and material shall be secured to the skid platform or pallet base, braced and blocked or separated within the container. Care should be taken to protect finish painted items.

12.2

e)

Equipment shall be adequately prepared to provide against entry of dust, sand and water during shipment. Small items shall be sealed with plastic containers.

f)

Assembly drawings required shall accompany the shipment. These shall be properly identified and be packed to prevent damage in shipment or in handling and unpacking the equipment

General Preservation Requirements a)

In general, application of rust preventatives to alloy and non-corrodible equipment and materials is not required. Stainless steel items may require special treatment to prevent stress corrosion, especially when exposed to salty atmosphere.

b) A list of the specific rust preventatives used to protect the equipment shall be enclosed in the shipping container. c)

The manufacturer shall provide any special instruction deemed necessary for the removal or replacement of any rust preventatives, together with any special precautions to be taken during the period of storage. If special removal solvents are necessary, these shall be provided with the equipment.

d) After the hydrostatic test the equipment shall be cleaned and dried (no water pockets) prior to application of rust preventatives and shall be type A coated. e)

External machine-finish surfaces shall be type B or C coated as applicable.

f)

All flanged openings of mechanical equipment, 6 inch and larger shall be fitted with gasket and metal closures. Wooden closures, if agreed to be acceptable, shall be metal cross-braced and securely bolted or clamped on.

g) The cover and gasket size shall match the flange outside diameter. h) Gaskets shall be 1/8-inch minimum thickness rubber or neoprene. i)

The cover thickness and bolting size and number of bolts used shall be such that the cover effectively seals the flanged opening. The use of plastic Snap-On covers is acceptable on 4 inch and smaller openings.

j)

All threaded connections such as vents, drains, conduit, and piping connections shall be capped or plugged with metal or plastic materials after application of type A rust preventative.

k) All engaged and exposed threads; especially those used for flange protection shall be coated with a grease base rust preventative, type C.

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February, 2007


SUITABLE RUST PREVENTATIVES

A (oil)

B (Hard Film)

C (Soft Film)

Lube Oil Base

Asphalt Base

Grease Base

TYPICAL USE:

Interior Surfaces of mechanical, e.g. bearing, cylinders, etc

Machined Surface e.g. flange faces, etc

Where removal is difficult or a lubricating service is required.

ENJAY

Rust-ban

Rust-ban

Rust-ban

(HUMBLE)

339

373

394

SHELL

Ensis Engine Oil 30

Ensis 264

Ensis 210

MOBIL

Mobilarma 524

Mobilarma 633

Mobilarma 247

TEXACOP

Preservative Oil 30

Texacoat

Rustproof Compound H

VAVOLINE

Tectyl 876

Tectyl 890

Tectyl 853

BP

Energol Protective Oil 30

Energol CPD 33 or CPF 11

Energrease PR2 or CPC 41

TYPE

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February, 2007


Deliverable Schedule Delivery of Documents for Review

Document Description S/N

Required by

1 2 3

Vendor document Schedule

2WAFO

Engineering, Procurement and Manufacturing Schedule Sub order schedule

2WAFO

4 5

Outline & GA Drawings Tabulations of allowable nozzle loads

2WAFO

6 7 8 9 10

Weld Maps Weld procedure specifications and qualifications. NDE Procedures and completed summary sheet Surface preparation, painting and repair procedure Hydro test procedures

3WPTP

11 12 13

Performance test results Technical operating and maintenance manual Maintenance data sheet

6WAFO

14 15 16

Functional and performance test procedures Preparation for shipping and handling procedures Precommissioning / commissioning procedures

4WAFO

17 18

Quality Manual Quality control plan

WAFO LEGEND: ABBREVIATIONS USED WPTP IN COLUMN 3 WPTT WAT

SPDC- PP- 2007-02-00000244

2WAFO

2WAFO

3WPTP 3WPTP 3WAFO 3WPTP 1WAT 6WAFO

3WPTT 4WAFO 4WAFO 4WAFO

- Weeks After Firm Order - Weeks Prior To Production - Weeks Prior To Test

WPTD AIR WAIR Release

- Weeks Prior To Delivery - At Inspection Release - Weeks After Inspection

- Weeks After Test

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February, 2007


14.0

ATTACHMENTS – FACILITY DATA SHEETS

14.1

1x 20’’ Receiver at Keremo M/F

14.2

1x 8’’ Receiver for 8” Delivery line from Odidi 1 F/S

14.3

1x 8” Launcher at Odidi 1 F/S

14.4

1x 20’’ Launcher at Egwa 2/Odidi2 Pigging M/F to Keremo M/F

14.5

1x 16’’ Receiver at Egwa2/Odidi2 MF for 16” trunk line from Jones Creek

14.6

1x 8’’ Receiver at Egwa2/Odidi2 M/F for 8” delivery line from Egwa2 F/S

14.7

1x 8’’ Launcher at Egwa 2 F/S

14.8

1x 8’’ Receiver at Egwa2/Odidi2 MF for 8” delivery line from Odidi 2 F/S

14.9

1x 8’’ Launcher at Odidi 2 F/S

14.10

1x 8’’ Receiver at Egwa 1 MF for 8” delivery line from Egwa 1 F/S

14.11

1x 8’’ Launcher at Egwa 1 F/S

14.12

1x 8’’ Launcher at Batan F/S

14.13

1x 8’’ Receiver at Batan M/F for 8” Delivery line from Batan FS

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February, 2007


Principal:

SPDC Pipeline Systems / PPM

Pipeline:

20’’ TRUNKLINE LINE AT KEREMO MANIFOLD

Segment /Location:

20’’ RECEIVER AT KEREMO MANIFOLD

SPDC Drawing Number:

N/A

VIEW

PIPELINE

N5

N8

N3 N6

N7

N4

D

N2

C

N9

E

G

N10

F

N12 N11

N11

B

1

Hatch Type / Duty

2 3

N1

A

Normal / cleaning duty:

RECIEVER

Inspection duty:

O.L.I.

Size

Connection

Nozzle Schedule

4

N1

Pipeline

20’’ NS

ANSI Class 600 RF WNF

5

N2

Vent

2’’ NS

ANSI Class 600RF

6

N3

Instrument

2’’ NS

ANSI Class 600RF

7

N4

Balance Line

4” NS

ANSI Class 600RF

8

N5

Spare

2’’ NS

ANSI Class 600RF

9

N6

Safety Relief Valve

2’’ NS

ANSI Class 600RF

10

N7

Vent

2’’ NS

ANSI Class 600RF

11

N8

Spare

Not Applicable

Not Applicable

12

N9

End Closure

24’’ NS

Quick Release – Vertical Plane

13

N10

Drain

4’’ NS

ANSI Class 600RF

14

N11

Kicker

10’’ NS

ANSI Class 600RF

15

N12

Drain

4’’NS

ANSI Class 600RF

16

N4 / N11Balance/Kicker line orientation viewed from end closure end

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9 O’clock February, 2007

Pig Launcher and Receiver Specification Minor Barrel length

A

1500 mm

Major Barrel length

B

TBA

19

Reducer to kicker CL

C

TBA

20

End closure to kicker CL

D

1500 mm

17 Critical Dimensions

18

E

Major Barrel Nominal Diameter (API 5L X 52)

24’’NS

F

Minor Barrel Nominal Diameter (API 5L X 52)

20’’NS

G

Reducer (API 5L X 52)

21

Design Pressure

22

Design Temperature

23

Corrosion allowance

24

Connecting Pipeline details

25

Matching Pipe Outer Diameter

26

Nominal wall thickness

27

Maximum operating pressure (MAOP)

28

Process fluid

Stabilised Crude

29

Design Life

25 Years

24’’x 20’’ 1087.8 psi Min:

-10 C

+ 80 C 2 mm (max)

Prepared By:

Andrew Wilson

Date:

15 Feb 2007

Checked By:

Kamal Jangra

Date:

15 Feb 2007

Datasheet Ref:

Max:

SPDC-2007-02-00000244 / 011

Revision

20

Inch

7.925

mm

960

psi

1

Additional Notes: As part of the Pipeline Re-Entry Repair Project – manifold piping layout has been optimised to meet the current standards and operating regime.

A. Refer to Specification SPDC-PP-2007-02-00000244 / DEP 31.40.10.13.Gen B. In some cases original manifold system layout as been modified from existing drawings C. The distance between branch connections should be addressed to ensure it does not coincide with the pig cup/disc separation sequence as this may result in pig stoppage

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February, 2007


Principal:


Pipeline:

8’’ DELIVERY LINE FROM ODID1 FLOW STATION

Segment /Location:

8’’ RECEIVER AT ODIDI1 TIE-IN PIGGING MANIFOLD


N/A

VIEW

PIPELINE

N5

N8

N3 N6

N7

N4

D

N2

C

N9

G

E

N10

F

N12

N11

B

1

Hatch Type / Duty

2 3

Nozzle Schedule

N1

N11

A


RECEIVER

Inspection duty:

O.L.I

Size

Connection ANSI Class 600 RF WNF

4

N1

Pipeline

5

N2

Vent

8’’ NS 2” NS

6

N3

Instrument

2” NS

ANSI Class 600RF ANSI Class 600RF

ANSI Class 600RF

7

N4

Pig Signaler

2” NS

8

N5

Spare

2’’ NS

ANSI Class 600RF

9

N6

Safety Relief Valve

2’’ NS

ANSI Class 600RF

10

N7

Vent

2’’ NS

ANSI Class 600RF

11

N8

Spare

2’’ NS

ANSI Class 600RF

12

N9

End Closure

10’’ NS

13

N10

Drain

4’’NS

Quick Release – Vertical Plane ANSI Class 600RF

14

N11

Kicker

4’’ NS

ANSI Class 600RF

15

N12

Drain

4’’ NS

ANSI Class 600RF

SPDC- PP- 2007-02-00000244

Page 18 of 41

February, 2007

Pig Launcher and Receiver Specification Kicker line orientation viewed from end closure end

16

3 O’clock

Minor Barrel length

A

3900 mm (min)

Major Barrel length

B

TBA

19


C

TBA

20


D

3900 mm (min)


18

E


10’’ NS

F


8’’ NS

G


21

Design Pressure

22

Design Temperature

23

Corrosion allowance

24


25


26


27


28

Process fluid

Stabilised Crude

29

Design Life

25 Years

10’’ x 8’’ 1350 psi Min:

-10 C

+ 80 C 2 mm (max)

Prepared By:

Andrew Wilson

Date:

15 Feb 2007

Checked By:

Kamal Jangra

Date:

15 Feb 2007

Datasheet Ref:

Max:

SPDC-2007-02-00000244/ 006

Revision

8

Inch

8.179

mm

960

psi

A1

Additional Notes: As part of the Pipeline Re-Entry Repair Project – manifold piping layout has been optimised to meet the current standards and operating regime. A. Refer to Specification SPDC-PP-2007-02-00000244 / DEP 31.40.10.13.Gen B. In some cases original manifold system layout as been modified from existing drawings C. Modification 2nd kicker line at 344mm should be removed. D. The distance between branch connections should be addressed to ensure it does not coincide with the pig cup/disc separation sequence as this may result in pig stoppage

SPDC- PP- 2007-02-00000244

Page 19 of 41

February, 2007


Principal:


Pipeline:

8’’ DELIVERY LINE FROM ODID1 FLOW STATION

Segment /Location:

8’’ LAUNCHER AT ODIDI1 FLOW STATION


N/A

VIEW

PIPELINE

N5

N8

N3 N6

N7

N4

D

N2

C

N9

G

E

N10

F

N12

N11

B

1

Hatch Type / Duty

2 3

Nozzle Schedule

N1

N11

A


LAUNCHER

Inspection duty:

O.L.I

Size

Connection ANSI Class 600 RF WNF

4

N1

Pipeline

5

N2

Vent

8’’ NS 2” NS

6

N3

Instrument

2” NS


ANSI Class 600RF

7

N4

Pig Signaler

2” NS

8

N5

Spare

2’’ NS

ANSI Class 600RF

9

N6

Safety Relief Valve

2’’ NS

ANSI Class 600RF

10

N7

Vent

2’’ NS

ANSI Class 600RF

11

N8

Spare

2’’ NS

ANSI Class 600RF

12

N9

End Closure

10’’ NS

13

N10

Drain

4’’NS


14

N11

Kicker

4’’ NS

ANSI Class 600RF

15

N12

Drain

4’’ NS

ANSI Class 600RF

SPDC- PP- 2007-02-00000244

Page 20 of 41

February, 2007


16

3 O’clock

Minor Barrel length

A

1500 mm (min)

Major Barrel length

B

4100 mm (min)

19


C

TBA

20


D

TBA


18

E


10’’ NS

F


8’’ NS

G


21

Design Pressure

22

Design Temperature

23

Corrosion allowance

24


25


26


27


28

Process fluid

Stabilised Crude

29

Design Life

25 Years

10’’ x 8’’ 1350 psi Min:

-10 C

+ 80 C 2 mm (max)

Prepared By:

Andrew Wilson

Date:

14 March 2007

Checked By:

Kamal Jangra

Date:

14 March 2007

Datasheet Ref:

Max:

SPDC-2007-02-00000244/ 012

Revision

8

Inch

8.179

mm

960

psi

A1

Additional Notes: As part of the Pipeline Re-Entry Repair Project – manifold piping layout has been optimised to meet the current standards and operating regime. A. Refer to Specification SPDC-PP-2007-02-00000244 / DEP 31.40.10.13.Gen B. In some cases original manifold system layout as been modified from existing drawings C. The distance between branch connections should be addressed to ensure it does not coincide with the pig cup/disc separation sequence as this may result in pig stoppage

SPDC- PP- 2007-02-00000244

Page 21 of 41

February, 2007


Principal:


Pipeline:

20’’ TRUNKLINE LINE EGWA2/ODIDI2 PIGGING MF TO KEREMO MANIFOLD

Segment /Location:

20’’ LAUNCHER AT EGWA 2 ODIDI 2 PIGGING MANIFOLD


N/A

VIEW

PIPELINE

N5

N8

N3 N6

N7

N4

D

N2

C

N9

E

G

N10

F

N12N11

N11

B

1

Hatch Type / Duty

2 3

N1

Nozzle Schedule

A


LAUNCHER

Inspection duty:

O.L.I.

Size

Connection ANSI Class 600 RF WNF ANSI Class 600RF

4

N1

Pipeline

20’’ NS

5

N2

Vent

2’’ NS

6

N3

Instrument

ANSI Class 600RF

7

N4

Balance Line

2’’ NS 4” NS

8

N5

Spare

2’’ NS

ANSI Class 600RF

9

N6

Safety Relief Valve

2’’ NS

ANSI Class 600RF

10

N7

Vent

2’’ NS

ANSI Class 600RF

11

N8

Spare

Not Applicable

Not Applicable

12

N9

End Closure

24’’ NS

13

N10

Drain

4’’NS


14

N11

Kicker

10’’ NS

ANSI Class 600RF

15

N12

Drain

4’’NS

ANSI Class 600RF

SPDC- PP- 2007-02-00000244

Page 22 of 41

ANSI Class 600RF

February, 2007

Pig Launcher and Receiver Specification N4 / N11Balance/Kicker line orientation viewed from end closure end

16

3 O’clock

Minor Barrel length

A

1500 mm

Major Barrel length

B

5100 mm

19


C

TBA

20


D

TBA


18

E


24’’NS

F


20’’NS

G


21

Design Pressure

22

Design Temperature

23

Corrosion allowance

24


25


26


27


28

Process fluid

Stabilised Crude

29

Design Life

25 Years

24’’x 20’’ 1087.8 psi Min:

-10 C

+ 80 C 2 mm (max)

Prepared By:

Andrew Wilson

Date:

15 Feb 2007

Checked By:

Kamal Jangra

Date:

15 Feb 2007

Datasheet Ref:

Max:

SPDC-2007-02-00000244 / 004

Revision

20

Inch

7.925

mm

960

psi

1

Additional Notes: As part of the Pipeline Re-Entry Repair Project – manifold piping layout has been optimised to meet the current standards and operating regime. A. Refer to Specification SPDC-PP-2007-02-00000244 / DEP 31.40.10.13.Gen B. In some cases original manifold system layout as been modified from existing drawings C. On kicker line the Conical 10’’ x 8’’ reducer is to be standardised to 8’’ weldolet connection D. The distance between branch connections should be addressed to ensure it does not coincide with the pig cup/disc separation sequence as this may result in pig stoppage

SPDC- PP- 2007-02-00000244

Page 23 of 41

February, 2007


Principal:


Pipeline:

16’’ TRUNK LINE FROM JONES CREEK FLOW STATION

Segment /Location:

16” RECIEVER AT EGWA 2/ODIDI 2 PIGGING MANIFOLD


NA

VIEW

PIPELINE N5

N8

N3 N6

N7

N4

D

N2

C

N9

E

G

N10

F

N12 N11

N11

B

1

Hatch Type / Duty

2 3

Nozzle Schedule

N1

A


RECEIVER

Inspection duty:

O.L.I

Size


4

N1

Pipeline

16’’ NS

5

N2

Vent

2’’ NS

6

N3

Instrument

ANSI Class 600RF

7

N4

Balance Line

2’’ NS 4 ” NS

8

N5

Spare

2’’ NS

ANSI Class 600RF

9

N6

Safety Relief Valve

2’’ NS

ANSI Class 600RF

10

N7

Vent

2’’ NS

ANSI Class 600RF

11

N8

Spare

2’’ NS

ANSI Class 600RF

12

N9

End Closure

18’’ NS

13

N10

Drain

4’’NS


14

N11

Kicker

8’’ NS

ANSI Class 600RF

15

N12

Drain

4’’ NS

ANSI Class 600RF

SPDC- PP- 2007-02-00000244

Page 24 of 41

ANSI Class 600RF

February, 2007

Pig Launcher and Receiver Specification 16

N4 / N11Balance/Kicker line orientation viewed from end closure end

9 O’clock

Minor Barrel length

A

5100mm

Major Barrel length

B

TBA

19


C

TBA

20


D

5100mm

17 18

Critical Dimensions

E


18’’NS

F


16’’NS

G


21

Design Pressure

22

Design Temperature

23

Corrosion allowance

24


25


26


27


28

Process fluid

Stabilised Crude

29

Design Life

25 Years

18’’x16’’ 1087.8 psi Min:

-10 C

+ 80 C 2 mm (max)

Prepared By:

Andrew Wilson

Date:

15 Feb 2007

Checked By:

Kamal Jangra

Date:

15 Feb 2007

Datasheet Ref:

Max:

SPDC-2007-02-00000244 / 007

Revision

16

Inch

7.925

Mm

960

Psi

1

Additional Notes: As part of the Pipeline Re-Entry Repair Project – manifold piping layout has been optimised to meet the current standards and operating regime. A. Refer to Specification SPDC-PP-2007-02-00000244 / DEP 31.40.10.13.Gen B. In some cases original manifold system layout as been modified from existing drawings C. Modification Minor barrel to pipeline connection is to be changed to flanged connection D. Modification removed the 6’’ Kicker line located at 1meter from the reducer towards end closure E. The distance between branch connections should be addressed to ensure it does not coincide with the pig cup/disc separation sequence as this may result in pig stoppage

SPDC- PP- 2007-02-00000244

Page 25 of 41

February, 2007


Principal:


Pipeline:

8’’ DELIVERY LINE FROM EGWA 2 FLOW STATION

Segment /Location:

8’’ RECEIVER AT EGWA 2/ODIDI 2 PIGGING MANIFOLD


N/A

VIEW

PIPELINE

N5

N8

N3 N6

N7

N4

D

N2

C

N9

E

G

N10

F

N12

N11

N11

B

1

A


Hatch Type / Duty

Inspection duty:

2 3

Nozzle Schedule

N1

RECEIVER O.L.I

Size


4

N1

Pipeline

8’’ NS

5

N2

Vent

2’’ NS

6

N3

Instrument

ANSI Class 600RF

7

N4

Pig Signaler

2’’ NS 2” NS

8

N5

Spare

2’’ NS

ANSI Class 600RF

9

N6

Safety Relief Valve

2’’ NS

ANSI Class 600RF

10

N7

Vent

2’’ NS

ANSI Class 600RF

11

N8

Spare

2’’ NS

ANSI Class 600RF

12

N9

End Closure

10’’ NS

13

N10

Drain

4’’NS


14

N11

Kicker

4’’ NS

ANSI Class 600RF

15

N12

Drain

4’’ NS

ANSI Class 600RF

SPDC- PP- 2007-02-00000244

Page 26 of 41

ANSI Class 600RF

February, 2007


16

3 O’clock

Minor Barrel length

A

3900 mm (min)

Major Barrel length

B

TBA

19


C

TBA

20


D

3900 mm (min)


18

E


10’’ NS

F


8’’ NS

G


21

Design Pressure

22

Design Temperature

23

Corrosion allowance

24


25


26

10’’ x 8’’ 1440 psi Min:

-10 C

Max:

+ 80 C 2 mm (max)

8

Inch


6.35

mm

27


960

psi

28

Process fluid

Stabilised Crude

29

Design Life

25 Years

Prepared By:

Andrew Wilson

Date:

15 Feb 2007

Checked By:

Kamal Jangra

Date:

15 Feb 2007

Datasheet Ref:

SPDC-2007-02-00000244 / 002

Revision

1

Additional Notes: As part of the Pipeline Re-Entry Repair Project – manifold piping layout has been optimised to meet the current standards and operating regime. A. Refer to Specification SPDC-PP-2007-02-00000244 / DEP 31.40.10.13.Gen B. In some cases original manifold system layout as been modified from existing drawings The distance between branch connections should be addressed to ensure it does not coincide with the pig cup/disc separation sequence as this may result in pig stoppage

SPDC- PP- 2007-02-00000244

Page 27 of 41

February, 2007


Principal:


Pipeline:

8’’ DELIVERY LINE FROM EGWA 2 FLOW STATION

Segment /Location:

8’’ LAUNCHER AT EGWA 2 FLOW STATION


N/A

VIEW

PIPELINE

N5

N8

N3 N6

N7

N4

D

N2

C

N9

G

E

N10

N12 N11

N11

B

1

Hatch Type / Duty

2 3

Nozzle Schedule

N1

F

A


LAUNCHER

Inspection duty:

O.L.I

Size

Connection

4

N1

Pipeline

8’’ NS

5

N2

Vent

2’’ NS

ANSI Class 600 RF WNF ANSI Class 600RF

6

N3

Instrument

7

N4

Pig Signaler

2” NS 2” NS


8

N5

Spare

2’’ NS

ANSI Class 600RF

9

N6

Safety Relief Valve

2” NS

10

N7

Vent

2’’ NS


11

N8

Spare

2’’ NS

ANSI Class 600RF

12

N9

End Closure

10’’ NS

13

N10

Drain

4’’NS


14

N11

Kicker

4’’NS

ANSI Class 600RF

15

N12

Drain

4’’NS

ANSI Class 600RF

SPDC- PP- 2007-02-00000244

Page 28 of 41

February, 2007


16

9 O’clock

Minor Barrel length

A

1500 mm (min)

Major Barrel length

B

4100 mm (min)

19


C

TBA

20


D

TBA

17 18

Critical Dimensions

E


10’’ NS

F


8’’ NS

G


10’’x 8’’

21

Design Pressure

1440 psi

22

Design Temperature

23

Corrosion allowance

24


25


26


27


960 psi

28

Process fluid

Stabilised Crude

29

Design Life

25 Years

Min:

-10 C

+ 80 C 2 mm (max)

Prepared By:

Andrew Wilson

Date:

15 Feb 2007

Checked By:

Kamal Jangra

Date:

15 Feb 2007

Datasheet Ref:

Max:

SPDC-2007-02-00000244/ 009

Revision

8

Inch

6.35

mm

1

Additional Notes: As part of the Pipeline Re-Entry Repair Project – manifold piping layout has be optimised to meet the current standards and operating regime. A. Refer to Specification SPDC-PP-2007-02-00000244 / DEP 31.40.10.13.Gen B. The distance between branch connections should be addressed to ensure it does not coincide with the pig cup/disc separation sequence as this may result in pig stoppage

SPDC- PP- 2007-02-00000244

Page 29 of 41

February, 2007


Principal: SPDC Pipeline Systems / PPM Pipeline:

8’’ DELIVERY LINE FROM ODIDI 2 FLOW STATION

Segment /Location:

8’’ RECEIVER AT EGWA 2/ODIDI 2 PIGGING MANIFOLD


N/A

VIEW

PIPELINE

N5

N8

N3 N6

N7

N4

D

N2

C

N9

E

N10

G

N12

N11

N11

B

1

Hatch Type / Duty

2 3

Nozzle Schedule

N1

F

A


RECEIVER

Inspection duty:

O.L.I

Size


4

N1

Pipeline

8’’ NS

5

N2

Vent

2’’ NS

6

N3

Instrument

ANSI Class 600RF

7

N4

Pig Signaler

2’’ NS 2” NS

8

N5

Spare

2’’ NS

ANSI Class 600RF

9

N6

Safety Relief Valve

2’’ NS

ANSI Class 600RF

10

N7

Vent

2’’ NS

ANSI Class 600RF

11

N8

Spare

2’’ NS

ANSI Class 600RF

12

N9

End Closure

10’’ NS

13

N10

Drain

4’’NS


14

N11

Kicker

4’’ NS

ANSI Class 600RF

15

N12

Drain

4’’NS

ANSI Class 600RF

SPDC- PP- 2007-02-00000244

Page 30 of 41

ANSI Class 600RF

February, 2007


16

9 O’clock

Minor Barrel length

A

3900 mm (min)

Major Barrel length

B

TBA

19


C

TBA

20


D

3900 mm (min)


18

E


10’’ NS

F


8’’ NS

G


21

Design Pressure

22

Design Temperature

23

Corrosion allowance

24


25


26

10’’ x 8’’ 1440 psi Min:

-10 C

Max:

+ 80 C 2 mm (max)

8

Inch


6.35

Mm

27


960

psi

28

Process fluid

Stabilised Crude

29

Design Life

25 Years

Prepared By:

Andrew Wilson

Date:

15 Feb 2007

Checked By:

Kamal Jangra

Date:

15 Feb 2007

Datasheet Ref:

SPDC-2007-02-00000244 / 003

Revision

1

Additional Notes: As part of the Pipeline Re-Entry Repair Project – manifold piping layout has been optimised to meet the current standards and operating regime. A. Refer to Specification SPDC-PP-2007-02-00000244 / DEP 31.40.10.13.Gen B. In some cases original manifold system layout as been modified from existing drawings C. Modification drain line incorporated at 6 o clock position on main barrel D. The distance between branch connections should be addressed to ensure it does not coincide with the pig cup/disc separation sequence as this may result in pig stoppage

SPDC- PP- 2007-02-00000244

Page 31 of 41

February, 2007


Principal:


Pipeline:

8’’ DELIVERY LINE FROM ODIDI 2 FLOW STATION

Segment /Location:

8’’ LAUNCHER AT ODIDI 2 FLOW STATION


N/A

VIEW

PIPELINE

N5

N8

N3 N6

N7

N4

D

N2

C

N9

G

E

N10

N12 N11

N11

B

1

Hatch Type / Duty

2 3

N1

F

Nozzle Schedule

A


LAUNCHER

Inspection duty:

O.L.I

Size

Connection

4

N1

Pipeline

8’’ NS

5

N2

Vent

2’’ NS


6

N3

Instrument

7

N4

Pig Signaler

2” NS 2” NS


8

N5

Spare

2’’ NS

ANSI Class 600RF

9

N6

Safety Relief Valve

2” NS

10

N7

Vent

2’’ NS


11

N8

Spare

2’’ NS

ANSI Class 600RF

12

N9

End Closure

10’’ NS

13

N10

Drain

4’’NS


14

N11

Kicker

4’’NS

ANSI Class 600RF

SPDC- PP- 2007-02-00000244

Page 32 of 41

February, 2007


N12

Drain

ANSI Class 600RF

4’’NS

Kicker line orientation viewed from end closure end

16

9 O’clock

Minor Barrel length

A

1500 mm (min)

Major Barrel length

B

4100 mm (min)

19


C

TBA

20


D

TBA

17 18

Critical Dimensions

E


10’’ NS

F


8’’ NS

G


10’’x 8’’

21

Design Pressure

1440 psi

22

Design Temperature

23

Corrosion allowance

24


25


26


27


960 psi

28

Process fluid

Stabilised Crude

29

Design Life

25 Years

Min:

-10 C

+ 80 C 2 mm (max)

Prepared By:

Andrew Wilson

Date:

00 Feb 2007

Checked By:

Kamal Jangra

Date:

00 Feb 2007

Datasheet Ref:

Max:

SPDC-2007-02-00000244/ 010

Revision

8

Inch

8.179

mm

1

Additional Notes: As part of the Pipeline Re-Entry Repair Project – manifold piping layout has be optimised to meet the current standards and operating regime. A. Refer to Specification SPDC-PP-2007-02-00000244 / DEP 31.40.10.13.Gen B. The distance between branch connections should be addressed to ensure it does not coincide with the pig cup/disc separation sequence as this may result in pig stoppage

SPDC- PP- 2007-02-00000244

Page 33 of 41

February, 2007



8’’ DELIVERY LINE FROM EGWA1 FLOW STATION

Segment /Location:

8’’ RECEIVER AT EGWA1 TIE-IN PIGGING MANIFOLD


N/A

VIEW

PIPELINE

N5

N8

N3 N6

N7

N4

D

N2

C

N9

E

F

G

N1

N12 N10

N11

N11

B

1

Hatch Type / Duty

2 3

Nozzle Schedule

A


RECEIVER

Inspection duty:

O.L.I

Size


4

N1

Pipeline

8’’ NS

5

N2

Vent

6

N3

Instrument

2’’ NS 2” NS

7

N4

Pig Signaler

2” NS

ANSI Class 600RF

8

N5

Spare

2’’ NS

ANSI Class 600RF

9

N6

Safety Relief Valve

2’’ NS

ANSI Class 600RF

10

N7

Vent

2’’ NS

ANSI Class 600RF

11

N8

Spare

2’’ NS

ANSI Class 600RF

12

N9

End Closure

10’’ NS

13

N10

Drain

4’’NS


14

N11

Kicker

4’’ NS

ANSI Class 600RF

15

N12

Drain

4”NS

ANSI Class 600RF

SPDC- PP- 2007-02-00000244

Page 34 of 41

ANSI Class 600RF

February, 2007


16

3 O’clock

Minor Barrel length

A

3900 mm (min)

Major Barrel length

B

TBA

19


C

TBA

20


D

3900 mm (min)


18

E


10’’ NS

F


8’’ NS

G


21

Design Pressure

22

Design Temperature

23

Corrosion allowance

24


25


26


27


28

Process fluid

Stabilised Crude

29

Design Life

25 Years

10’’ x 8’’ 1350 psi Min:

-10 C

+ 80 C 2 mm (max)

Prepared By:

Andrew Wilson

Date:

15 Feb 2007

Checked By:

Kamal Jangra

Date:

15 Feb 2007

Datasheet Ref:

Max:

SPDC-2007-02-00000244/ 005

Revision

8

Inch

8.179

mm

960

psi

1

Additional Notes: As part of the Pipeline Re-Entry Repair Project – manifold piping layout has been optimised to meet the current standards and operating regime. A. Refer to Specification SPDC-PP-2007-02-00000244 / DEP 31.40.10.13.Gen B. In some cases original manifold system layout as been modified from existing drawings C. Kicker line re positioned closer to end closure to facilitate launching and receiving D. The distance between branch connections should be addressed to ensure it does not coincide with the pig cup/disc separation sequence as this may result in pig stoppage

SPDC- PP- 2007-02-00000244

Page 35 of 41

February, 2007



8’’ DELIVERY LINE FROM EGWA1 FLOW STATION

Segment /Location:

8’’ LAUNCHER AT EGWA1 FLOW STATION


N/A

VIEW

PIPELINE

N5

N8

N3 N6

N7

N4

D

N2

C

N9

E

F

G

N1

N12 N10

N11

N11

B

1

Hatch Type / Duty

2 3

Nozzle Schedule

A


LAUNCHER

Inspection duty:

O.L.I

Size


4

N1

Pipeline

8’’ NS

5

N2

Vent

6

N3

Instrument

2’’ NS 2” NS

7

N4

Pig Signaler

2” NS

ANSI Class 600RF

8

N5

Spare

2’’ NS

ANSI Class 600RF

9

N6

Safety Relief Valve

2’’ NS

ANSI Class 600RF

10

N7

Vent

2’’ NS

ANSI Class 600RF

11

N8

Spare

2’’ NS

ANSI Class 600RF

12

N9

End Closure

10’’ NS

13

N10

Drain

4’’NS


14

N11

Kicker

4’’ NS

ANSI Class 600RF

15

N12

Drain

4”NS

ANSI Class 600RF

SPDC- PP- 2007-02-00000244

Page 36 of 41

ANSI Class 600RF

February, 2007


16

3 O’clock

Minor Barrel length

A

1500 mm (min)

Major Barrel length

B

4100 mm (min)

19


C

TBA

20


D

TBA


18

E


10’’ NS

F


8’’ NS

G


21

Design Pressure

22

Design Temperature

23

Corrosion allowance

24


25


26


27


28

Process fluid

Stabilised Crude

29

Design Life

25 Years

10’’ x 8’’ 1350 psi Min:

-10 C

+ 80 C 2 mm (max)

Prepared By:

Andrew Wilson

Date:

14 March 2007

Checked By:

Kamal Jangra

Date:

14 March 2007

Datasheet Ref:

Max:

SPDC-2007-02-00000244/ 013

Revision

8

Inch

8.179

mm

960

psi

1

Additional Notes: As part of the Pipeline Re-Entry Repair Project – manifold piping layout has been optimised to meet the current standards and operating regime. A. Refer to Specification SPDC- PP-2007-02-00000244 / DEP 31.40.10.13.Gen B. In some cases original manifold system layout as been modified from existing drawings C. The distance between branch connections should be addressed to ensure it does not coincide with the pig cup/disc separation sequence as this may result in pig stoppage

SPDC- PP- 2007-02-00000244

Page 37 of 41

February, 2007


Principal:


Pipeline:

8’’ BATAN DELIVERY LINE

Segment /Location:

8’’ LAUNCHER AT BATAN FLOW STATION


N/A

VIEW

PIPELINE

N5

N8

N3 N6

N7

N4

D

N2

C

N9

G

E

N10

F

N12 N11

N11

B

1

Hatch Type / Duty

2 3

Nozzle Schedule

N1

A


LAUNCHER

Inspection duty:

O.L.I

Size

Connection

4

N1

Pipeline

8’’ NS

5

N2

Vent

2’’ NS


6

N3

Instrument

7

N4

Pig Signaler

2” NS 2” NS


8

N5

Spare

2’’ NS

ANSI Class 600RF

9

N6

Safety Relief Valve

2” NS

10

N7

Vent

2’’ NS


11

N8

Spare

2’’ NS

ANSI Class 600RF

12

N9

End Closure

10’’ NS

13

N10

Drain

4’’NS


14

N11

Kicker

4’’NS

ANSI Class 600RF

SPDC- PP- 2007-02-00000244

Page 38 of 41

February, 2007


N12

Drain

ANSI Class 600RF

4’’NS


16

9 O’clock

Minor Barrel length

A

1500 mm (min)

Major Barrel length

B

4100 mm (min)

19


C

TBA

20


D

TBA

17 18

Critical Dimensions

E


10’’ NS

F


8’’ NS

G


10’’x 8’’

21

Design Pressure

1440 psi

22

Design Temperature

23

Corrosion allowance

24


25


26


27


960 psi

28

Process fluid

Stabilised Crude

29

Design Life

25 Years

Min:

-10 C

+ 80 C 2 mm (max)

Prepared By:

Andrew Wilson

Date:

00 Feb 2007

Checked By:

Kamal Jangra

Date:

00 Feb 2007

Datasheet Ref:

Ma x:

SPDC-2007-02-00000244/ 008

Revision

8

Inch

8.179

mm

1

Additional Notes: As part of the Pipeline Re-Entry Repair Project – manifold piping layout has be optimised to meet the current standards and operating regime. A. Refer to Specification SPDC- PP-2007-02-00000244 / DEP 31.40.10.13.Gen B. The distance between branch connections should be addressed to ensure it does not coincide with the pig cup/disc separation sequence as this may result in pig stoppage

SPDC- PP- 2007-02-00000244

Page 39 of 41

February, 2007


Principal:


Pipeline:

8’’ BATAN DELIVERY LINE FROM FLOW STATION

Segment /Location:

8’’ RECEIVER AT BATAN TIE IN PIGGING MANIFOLD


N/A

VIEW

PIPELINE

N5

N8

N3 N6

N7

N4

D

N2

C

N9

G

E

N10

F

N11

N11

N12

B

1

Hatch Type / Duty

2 3

N1

A


RECIEVER

Inspection duty:

O.L.I

Size

Connection

Nozzle Schedule

4

N1

Pipeline

8’’ NS

5

N2

Vent

2’’ NS


6

N3

Instrument

7

N4

Pig Signaler

2” NS 2” NS


8

N5

Spare

2’’ NS

ANSI Class 600RF

9

N6

Safety Relief Valve

2” NS

10

N7

Vent

2’’ NS


11

N8

Spare

2’’ NS

ANSI Class 600RF

12

N9

End Closure

10’’ NS

13

N10

Drain

4’’NS


14

N11

Kicker

4’’NS

ANSI Class 600RF

15

N12

Drain

4’’NS

16


SPDC- PP- 2007-02-00000244

Page 40 of 41

ANSI Class 600RF 3 O’clock February, 2007

Pig Launcher and Receiver Specification Minor Barrel length

A

3900 mm (min)

Major Barrel length

B

TBA

19


C

TBA

20


D

3900 mm (min)

17 18

Critical Dimensions

E


10’’ NS

F


8’’ NS

G


10’’x 8’’

21

Design Pressure

1440 psi

22

Design Temperature

23

Corrosion allowance

24


25


26


27


960 psi

28

Process fluid

Stabilised Crude

29

Design Life

25 Years

Min:

-10 C

+ 80 C 2 mm (max)

Prepared By:

Andrew Wilson

Date:

27 Feb 2007

Checked By:

Kamal Jangra

Date:

28 Feb 2007

Datasheet Ref:

Max:

SPDC-2007-02-00000244/ 001

Revision

8

Inch

8.179

mm

1

Additional Notes: As part of the Pipeline Re-Entry Repair Project – manifold piping layout has been optimised to meet the current standards and operating regime. A. Refer to Specification SPDC- PP-2007-02-00000244 / DEP 31.40.10.13.Gen B. Non intrusive Pig signalers to be utilized (Clamp on to reduce maintenance activities) C. The distance between branch connections should be addressed to ensure it does not coincide with the pig cup/disc separation sequence as this may result in pig stoppage

SPDC- PP- 2007-02-00000244

Page 41 of 41

February, 2007

Pig Launcher and Receiver Specification Rev 3

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