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This document contains proprietary information belonging to Maersk Oil and shall not be wholly or partially reproduced nor disclosed without prior written permission from Maersk Oil. MOG-EP-PIP-STD-0016 Rev 2.0 Technical Standard - MOTS-16 Valves Effective from: 10 th June 2013 1.0 10/02/2012 1 st Issue. Replaces TS-16, MITS-16 and MONS-T-09 2.0 10/06/2013 Changes as indicated Revision Date Notes Author: Focal point: Approved by: Approval Date: Lars Sielemann Jørn R. Pedersen Per Angelo 10 th June 2013

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  • This document contains proprietary information belonging to Maersk Oil and shall not be wholly or partially reproduced nor disclosed without prior written permission from Maersk Oil.

    MOG-EP-PIP-STD-0016 Rev 2.0

    Technical Standard - MOTS-16 Valves Effective from: 10th June 2013

    1.0 10/02/2012 1st Issue. Replaces TS-16, MITS-16 and MONS-T-09 2.0 10/06/2013 Changes as indicated

    Revision Date Notes

    Author: Focal point: Approved by: Approval Date:

    Lars Sielemann Jrn R. Pedersen Per Angelo 10th June 2013

  • This document contains proprietary information belonging to Maersk Oil and shall not be wholly or partially reproduced nor disclosed without prior written permission from Maersk Oil.

    MOG-EP-PIP-STD-0016 Rev 2.0

    Page 2 of 35

    Table of Contents

    1 Introduction ................................................................................................ 4

    2 Objective .................................................................................................... 4

    3 Scope ......................................................................................................... 4

    3.1 General ................................................................................................... 4

    3.2 Existing Facilities ...................................................................................... 4

    3.3 Deviations ............................................................................................... 4

    4 Terms and Definitions ................................................................................... 4

    5 Regulations, Codes and Standards .................................................................. 7

    5.1 Laws and Regulations ............................................................................... 7

    5.2 Codes and Standards ................................................................................ 8

    5.3 Company Standards, Procedures and Guidelines ......................................... 10

    6 Compatibility ............................................................................................. 10

    7 Specification .............................................................................................. 10

    8 Additional Requirements ............................................................................. 12

    8.1 Valves .................................................................................................. 12

    8.1.1 General Requirements ......................................................................... 12 8.1.1.1 Valve Signature .................................................................................. 13

    8.1.2 Ball Valves ......................................................................................... 13 8.1.3 Butterfly Valves .................................................................................. 14 8.1.4 Check Valves ..................................................................................... 14 8.1.5 Gate Valves ....................................................................................... 14 8.1.6 Globe Valves ...................................................................................... 15 8.1.7 Needle Valves .................................................................................... 15 8.1.8 Slim-line Double Block and Bleed Valves ................................................ 15 8.2 Actuators .............................................................................................. 15

    8.3 Actuated On/Off Valves (ESDV, BDV, XCV) ................................................. 16

    8.4 Riser Valves .......................................................................................... 18

    8.5 Control Valves (PCV, TCV, LCV, FCV, CVA) ................................................. 20

    8.6 Relief Valves .......................................................................................... 20

    8.7 Control Panels ........................................................................................ 21

    9 Materials ................................................................................................... 22

    9.1 General ................................................................................................. 22

    9.1.1 Non-Destructive Examination ............................................................... 22 9.1.2 Grease Nipple .................................................................................... 23 9.2 Production Testing .................................................................................. 23

    9.3 Forged Valves ........................................................................................ 23

  • This document contains proprietary information belonging to Maersk Oil and shall not be wholly or partially reproduced nor disclosed without prior written permission from Maersk Oil.

    MOG-EP-PIP-STD-0016 Rev 2.0

    Page 3 of 35

    9.3.1 General ............................................................................................. 23 9.3.2 Carbon Steel ...................................................................................... 23 9.3.3 Austenitic Stainless Steel Type 316/316L ............................................... 23 9.3.4 Austenitic Stainless Steel Type 6% Mo ................................................... 23 9.3.5 Duplex Stainless Steel Type 22% Cr ...................................................... 24 9.3.6 Duplex Stainless Steel Type 25% Cr ...................................................... 24 9.4 Cast Valves ........................................................................................... 24

    9.4.1 Representative Test Bar ....................................................................... 24 9.4.2 Weld Repair ....................................................................................... 24 9.4.3 Carbon Steel ...................................................................................... 24 9.4.4 Austenitic Stainless Steel Type 316/316L ............................................... 25 9.4.5 Austenitic Stainless Steel Type 6% Mo ................................................... 25 9.4.6 Duplex Stainless Steel Type 22% Cr ...................................................... 25 9.4.7 Duplex Stainless Steel Type 25% Cr ...................................................... 25 9.5 Modification ........................................................................................... 26

    9.6 Valve Bolting ......................................................................................... 26

    9.7 Gaskets, Seals and Packing Materials ........................................................ 27

    9.8 Actuator Bolting ..................................................................................... 27

    10 General Requirements ................................................................................ 27

    10.1 Pressure Testing .................................................................................... 27

    10.2 Painting ................................................................................................ 28

    10.3 Pickling and Passivation ........................................................................... 28

    11 Certification ............................................................................................... 28

    12 Documentation .......................................................................................... 29

    12.1 Drawings .............................................................................................. 29

    12.2 Riser Valves .......................................................................................... 29

    13 Attachments .............................................................................................. 29

    13.1 Attachment 1: Valve and Actuator Data Sheets ........................................... 29

    13.1.1 Actuators .......................................................................................... 29 13.1.2 Control Valves .................................................................................... 29 13.1.3 Pressure Safety Valves ........................................................................ 29 13.2 Attachment 2: Control Diagrams .............................................................. 29

    13.3 Attachment 3: Piping Specification ............................................................ 30

    13.4 Attachment 4: Valve Specification ............................................................. 30

    13.5 Attachment 5: Valve Selection Manual ....................................................... 30

    13.6 Attachment 6: Drawing of Typical NPT Threaded Connection Detail ................ 30

    14 Appendices................................................................................................ 30

    Appendix A BU Country Specific Requirements ................................................... 31

    Appendix B Material Data Sheet for Forgings and Castings ................................... 35

  • This document contains proprietary information belonging to Maersk Oil and shall not be wholly or partially reproduced nor disclosed without prior written permission from Maersk Oil.

    MOG-EP-PIP-STD-0016 Rev 2.0

    Page 4 of 35

    1 Introduction

    This technical standard defines the Maersk Oil requirements for valves.

    This standard forms part of the overall Maersk Oil Technical Standards (MOTS).

    The MOTS specify the following:

    Applicable codes and standards.

    Company requirements additional to applicable codes and standards specified.

    2 Objective

    The objective of this technical standard is to ensure a consistent design for the fabrication and installation of valves, across all new and existing Company facilities with regards to safety, the environment, operability and maintainability. 3 Scope

    3.1 General

    This technical standard shall apply to all new installations, and to modifications and extensions to existing Company facilities, both onshore and offshore. The standard shall apply during all project stages including, but not limited to, conceptual, FEED, detailed design, procurement, construction and commissioning.

    3.2 Existing Facilities

    When applying MOTS in connection with modifications and extensions to existing Company facilities built to other specifications, the user shall exercise engineering judgement necessary for ensuring compatibility with existing conditions, and ensure that the required quality and safety is achieved.

    However, this technical standard is not retroactive, although it may be used as a reference point for performing an audit or gap analysis of existing facilities. When significant deficiencies compared to industry practice and accepted safety levels, etc., are found on existing facilities, then the improvements shall comply with MOTS.

    3.3 Deviations

    Deviations from this technical standard shall not be permitted unless prior written approval is obtained from the relevant Technical Authority, in compliance with MOG-EP-GEN-PRO-0203: Technical Authority and Waiver Procedure. Proposals for deviations shall be prepared only when:

    Significant cost savings may be obtained without compromising on Health, Safety and Environment (HSE) and operability requirements;

    New experience shows that the requirements are not suitable for the design or work being performed;

    Concepts or requirements specified are not possible or feasible to fulfil, e.g. when modifying existing facilities.

    4 Terms and Definitions

    For the purpose of this standard, the following terms and definitions shall apply.

  • This document contains proprietary information belonging to Maersk Oil and shall not be wholly or partially reproduced nor disclosed without prior written permission from Maersk Oil.

    MOG-EP-PIP-STD-0016 Rev 2.0

    Page 5 of 35

    Terms

    May Used to indicate that a provision is optional, i.e. indicates a course of action permissible within the limits of the document Shall Used to indicate that a provision is a requirement, i.e. mandatory

    Should Used to indicate that a provision is a recommendation to be used as good practice, but is not mandatory Company Maersk Oil, including any of the BUs

    Contractor

    Party responsible for the design / construction / installation / commissioning of the facility including its employees, agents, subcontractors, suppliers, vendors, inspectors and other authorised representatives providing services to Contractor for any aspects of the work

    Facility Onshore plant or offshore fixed, floating or subsea unit, excluding mobile drilling units

    Certifying Agency

    A verifying body such as; American Bureau of Shipping (ABS) Lloyd's Register of Shipping (Lloyds) Bureau Veritas (BV) Det Norske Veritas (DNV)

    Low Temperature Design temperature below -10C

    Pressure containing and retaining parts

    Pressure containing and retaining parts include all metallic components that would cause a pressure release in the event of component failure. Pressure containing and retaining parts is defined in ASME PCC 25, sec. 2.4, which include, but are not limited to, body, end connectors, bonnet, bolting, stem and ball

    Riser XCV Actuated valve located in the riser section of a pipeline between the riser ESDV and a pig launcher or receiver

    Sour-Service

    H2S containing medium as defined by: ISO 15156-2, Annex A, SSC region 3 for C-Mn steel ISO 15156-3, Table A1 Any equipment/component for Corrosion Resistant Alloys (CRA) Note: Vendor shall ensure the material properties. Company shall verify fitness for service where installed

    Abbreviations

    AED Anti-Explosive Decompression

    API American Petroleum Institute

    ASME American Society of Mechanical Engineers

    ASTM American Society for Testing and Materials

    BU Business Unit

    C/C-Mn Carbon and Carbon-Manganese Steel

    C-Mn Carbon-Manganese Steel

    CE Conformit Europene (European Conformity)

    CRA Corrosion Resistant Alloys

    CS Carbon Steel

  • This document contains proprietary information belonging to Maersk Oil and shall not be wholly or partially reproduced nor disclosed without prior written permission from Maersk Oil.

    MOG-EP-PIP-STD-0016 Rev 2.0

    Page 6 of 35

    CV Valve Constant

    DBB Double Block and Bleed

    EN European Standards

    ESD Emergency Shutdown

    FCI Fluid Controls Institute

    FEED Front End Engineering Design

    FLT For Low Temperature

    HAZ Heat Affected Zones

    HIPS High Integrity Protection System

    HSE Health, Safety and Environment

    IGC Intergranular Corrosion

    ISO International Standards Organisation

    LTCS Low Temperature Carbon Steel

    MOTS Maersk Oil Technical Standard

    MODK Maersk Oil Denmark

    MOK Maersk Oil Kazakhstan

    MOA Maersk Oil Angola

    MOH Maersk Oil Houston

    MOQ Maersk Oil Qatar

    NB Nominal Bore

    NDE Non-Destructive Examination

    NPS Nominal Pipe Size

    NPT National Pipe Taper Thread (US standard for tapered piping thread)

    PO Purchase Order

    PREN Pitting Resistance Equivalent Number

    SCADA Supervisory Control and Data Acquisition

    SS Stainless Steel

    TA Technical Authority Valve Function Code

    BDV Blowdown Valve

    CHV Check Valve

    CVA Choke Valve (adjustable)

  • This document contains proprietary information belonging to Maersk Oil and shall not be wholly or partially reproduced nor disclosed without prior written permission from Maersk Oil.

    MOG-EP-PIP-STD-0016 Rev 2.0

    Page 7 of 35

    ESDV Emergency Shutdown Valve

    FCV Flow Control Valve

    FHCV Fire Hand Control Valve

    FSOV Fire Solenoid Valve

    HCV Hand Control Valve

    IBV Instrument Bleed Valve

    IIV Instrument Isolation Valve

    LCV Level Control Valve

    MCV Master Control Valve

    MOV Motor Operated Valve

    OSDV Operational Shutdown Valve

    OV Override Valve

    PCV Pressure Control Valve

    PIV Process Isolation Valve

    PRV Pressure Relief Valve

    PSV Pressure Safety Valve

    PV Pilot Valve

    SOV Solenoid Operated Valve

    SDBB Slim-line Double Block and Bleed Valve

    TCV Temperature Control Valve

    VPSV Vacuum Pressure Safety Valve

    XCV Operated Valve (should be Unclassified Valve (Actuator Activated Valve)) 5 Regulations, Codes and Standards

    All regulations, codes and standards referred to in this technical standard shall apply in the latest edition, unless otherwise specified.

    Appendix A lists any specific amendments to this standard, depending on Business Unit (BU) geographical locations.

    5.1 Laws and Regulations

    If the country of installation has laws and regulations related to the scope of this technical standard, then they shall be applied in addition to the requirements in this technical standard. In case of conflict, the most stringent requirements shall apply.

  • This document contains proprietary information belonging to Maersk Oil and shall not be wholly or partially reproduced nor disclosed without prior written permission from Maersk Oil.

    MOG-EP-PIP-STD-0016 Rev 2.0

    Page 8 of 35

    5.2 Codes and Standards

    Reference Title

    2006/42/EC Directive of the European Parliament and of the Council on Machinery

    ASME Section VIII Division 1 Rules for Construction of Pressure Vessels

    ASME B16.34 Valves Flanged, Threaded and Welding End

    ASME B16.10 Face to Face and End to End Dimensions of Valves

    ASME B16.5 Pipe Flanges and Flanged Fittings

    ASME B16.25 Butt Welding Ends

    ASME B31.3 Process Piping

    ASME PTC 25 Pressure Relief Devices

    ASTM A105 Standard Specification for Carbon Steel Forgings for Piping Applications

    ASTM A153 Standard Specification for Zinc Coating (Hot-Dip) on Iron and Steel Hardware

    ASTM A182 Standard Specification for Forged or Rolled Alloy and Stainless Steel Pipe Flanges, Forged Fittings, and Valves and Parts for High-Temperature Service

    ASTM A193 Standard Specification for Alloy-Steel and Stainless Steel Bolting Materials for High Temperature or High Pressure Service and Other Special Purpose Applications

    ASTM A194 Standard Specification for Carbon and Alloy Steel Nuts for Bolts for High Pressure or High Temperature Service, or Both

    ASTM A262 Standard Practices for Detecting Susceptibility to Intergranular Attack in Austenitic Stainless Steels

    ASTM A275 Standard Practice for Magnetic Particle Examination of Steel Forgings

    ASTM A276 Standard Specification for Stainless Steel Bars and Shapes

    ASTM A320 Standard Specification for Alloy-Steel and Stainless Steel Bolting for Low-Temperature Service

    ASTM A350 Standard Specification for and Low-Alloy Steel, Forgings, Requiring Notch Toughness Testing for Piping Components

    ASTM A351 Standard Specification for Castings, Austenitic, Austenitic-Ferrite (Duplex), for Pressure-Containing Parts

    ASTM A352 Standard Specification for Steel Castings, Ferrite and Martensitic, for Pressure-Containing Parts, Suitable for Low-Temperature Service

    ASTM A370 Standard Test Methods and Definitions for Mechanical Testing of Steel Products

  • This document contains proprietary information belonging to Maersk Oil and shall not be wholly or partially reproduced nor disclosed without prior written permission from Maersk Oil.

    MOG-EP-PIP-STD-0016 Rev 2.0

    Page 9 of 35

    Reference Title

    ASTM A488 Standard Practice for Steel Castings, Welding, Qualifications of Procedures and Personnel

    ASTM A609 Standard Practice for Castings, Carbon, Low-Alloy, and Martensitic Stainless Steel, Ultrasonic Examination Thereof

    ASTM A703 Standard Specification for Steel Castings, General Requirements, for Pressure Containing Parts

    ASTM A923 Standard Test Methods for Detecting Detrimental Intermetallic Phase in Wrought Duplex Austenitic/Ferrite Stainless Steels

    ASTM A961 Standard Specification for Common Requirements for Steel Flanges, Forged Fittings, Valves and Parts for Piping Applications

    ASTM A995 Standard Specification for Castings, Austenitic-Ferrite (Duplex) Stainless Steel, for Pressure-Containing Parts

    ASTM B633 Standard Specification for Electrodeposited Coatings of Zinc on Iron and Steel

    ASTM E165 Standard Test Method for Liquid Penetrant Examination

    ASTM E709 Standard Guide for Magnetic Particle Examination

    ASTM G48 Standard Test Methods for Pitting and Crevice Corrosion Resistance of Stainless Steels and Related Alloys by Use of Ferric Chloride Solutions

    ATEX 94/9/EC Atmospheric Explosive Directive. Equipment and Protective Systems Intended for Use in Potentially Explosive Atmospheres

    API RP 520 Sizing, Selection and Installation of Pressure-Relieving Devices in Refineries

    API RP 521 Guide for Pressure-Relieving and De-pressuring Systems

    API STD 526 Flanged Steel Pressure Relief Valves

    API STD 527 Seat Tightness of Pressure Relief Valves

    API STD 594 Check Valves: Flanged, Lug, Wafer and Butt Welding

    API STD 598 Valve Inspection and Testing

    API STD 599 Metal Plug Valves - Flanged, Threaded and Welding Ends

    API STD 600 Steel Gate Valves - Flanged and Butt-Welding Ends, Bolted Bonnets

    API STD 609 Butterfly Valves: Double-Flanged, Lug- and Wafer-Type

    API STD 2000 Venting Atmospheric and Low-Pressure Storage Tanks

    EN 12266-1 Industrial Valves. Testing of Valves. Pressure Tests, Test Procedures and Acceptance Criteria - Mandatory Requirements

    EN 12266-2 Industrial Valves. Testing of Valves. Tests, Test Procedures and Acceptance Criteria - Supplementary Requirements

  • This document contains proprietary information belonging to Maersk Oil and shall not be wholly or partially reproduced nor disclosed without prior written permission from Maersk Oil.

    MOG-EP-PIP-STD-0016 Rev 2.0

    Page 10 of 35

    Reference Title EN 10204 Metallic Products Types of Inspection Documents

    FCI 70-2 Control Valve Seat Leakage

    IEC 60534-2-1 Industrial Process Control Valves Part 2-1: Flow Capacity

    ISO 10434 (API 600) Bolted Bonnet Steel Gate Valves for the Petroleum, Petrochemical and Allied Industries

    ISO 10497 Testing of Valves Fire Type-Testing Requirements

    ISO 14313 (API 6D) Pipeline Transportation Systems - Pipeline Valves

    ISO 15156 /

    NACE MR 0175 Materials for Use in H2S-containing Environments in Oil and Gas Production

    PED 97/23/EC Pressure Equipment Directive

    5.3 Company Standards, Procedures and Guidelines

    Reference Title MOG-EP-INS-STD-0001 MOTS-01 Instrument Materials and Installation

    MOG-EP-PIP-STD-0002 MOTS-02 Piping Design and Materials

    MOG-EP-PIP-STD-0003 MOTS-03 Fabrication, Erection and Testing of Pipework

    MOG-EP-MET-STD-0012 MOTS-12 Welding and NDE of Welds

    MOG-EP-MET-STD-0034 MOTS-34 Protective External Coating of Steel

    MOG-EP-SAF-STD-0046 MOTS-46 High Integrity Protection Systems

    MOG-EP-GEN-PRO-0203 Technical Authority and Waiver Procedure 6 Compatibility

    When applying this MOTS for replacement and modification of components in existing Company facilities build to other specifications, there shall be exercised the necessary engineering judgement to ensure comparability between the replacement component and existing facilities. The component shall meet the required quality and safety requirements.

    7 Specification

    This standard does not cover: wellhead (API 6A) valves/actuators subsea valves/ actuators electrically operated actuators valves to be used inside accommodation and office facilities System requirements for HIPS; refer to MOG-EP-SAF-STD-0046:

    MOTS-46 High Integrity Protection Systems

    Valves and actuators shall be in compliance with this standard, using data sheets included in Attachment 1: Valve and Actuator Data Sheets.

  • This document contains proprietary information belonging to Maersk Oil and shall not be wholly or partially reproduced nor disclosed without prior written permission from Maersk Oil.

    MOG-EP-PIP-STD-0016 Rev 2.0

    Page 11 of 35

    The selected data sheet shall be completed by Company as a part of the contract or PO. On all data sheets, grey shaded boxes in the upper right corner shall be filled in (Predefined options).

    For valves, specification is complete hereafter (the valve is then described by the valve identification number; refer to 13.4 Attachment 4: Valve Specification).

    For safety critical valves, Emergency Shutdown (ESD) and Riser valves and actuators for these valves, data sheets shall be completed by the Company on a case by case basis filling in all outstanding data.

    Table 7-1 shows the data defined in the grey shaded boxes.

    On/Off Valves Actuators Control Valves Safety Valves Type of operation Valve Status Valve Spec 1 Valve Spec 1

    Process Specific Service Valve Function Valve Type 2 Valve Type 2 Single or Double Block 3 Valve Type Line Size Line Size

    Valve Size Valve Size Wall Thickness Valve Ends Valve Ends Valve Class Valve Ends Process Specific Service Valve Bore Operation Valve Pattern Duty

    Control System Process Specific Service

    Solenoid Voltage Operation Media Riser ESDV

    Notes: 1. Reference is made to MOG-EP-PIP-STD-0002: MOTS-02 Piping Design and Materials and

    Attachment 3: Piping Specification. 2. Reference is made to to Attachment 5: Valve Selection Manual. 3. Ball and plug valve data sheets only.

    Table 7-1 - Valve Specification Matrix

    All fields are self-explanatory except Process Specific Service. When selecting process specific service, the guideline shown in Table 7-2 shall be followed.

    Service Code Selected Service Code 1: General Service In all systems (Process and Utility) not mentioned below Service Code 2: Gas General In all gas lines not included in service code 3 Service Code 3: Gas High Temperature

    In all process gas lines downstream compressors upstream gas coolers

    Service Code 4: Process with Sand In all process lines upstream 1st stage separation In all produced water lines, where sand may be expected.

    Service Code 5: Water Injection In all water injection lines. Table 7-2 - Process Specific Service Guidelines

    A completed data sheet from valve supplier reflecting the actual valve delivery shall be forwarded to the Company for review and approval, prior to placing a PO. Deviations from the specified data sheet requirements or this technical standard, if any, shall be clearly marked in the column at the right side of the data sheet. This shall be compulsory for placing a PO. See also sections 11 Certification and 12 Documentation.

    For double block and bleed (DBB) ball or plug valves, additional specification sheets are available and shall be used for specification of operation type and orientation.

  • This document contains proprietary information belonging to Maersk Oil and shall not be wholly or partially reproduced nor disclosed without prior written permission from Maersk Oil.

    MOG-EP-PIP-STD-0016 Rev 2.0

    Page 12 of 35

    8 Additional Requirements

    This section specifies the common requirements to valves, actuators, control valves and control panels.

    Valves and actuators shall be designed, fabricated, tested, and documented in compliance with this technical specification and data sheets/drawings included in the appendices.

    If deviation between this specification and data sheets is found, the most stringent requirements shall apply. Mandatory requirements shall always be followed.

    8.1 Valves

    8.1.1 General Requirements

    Company may specify valve types which are outside the scope of this technical standard.

    Valve types not specified in this technical standard may be used subject to written Company approval (waiver request). In such cases, the valve specification requirements shall be agreed prior to placement of the PO.

    Ball, plug and gate valves shall be designed allowing design pressure to be applied from either end or from both ends simultaneously. Automatic internal bleeding of the cavity shall be required.

    Standard stock valves shall be designed to allow installation in any possible position. No restrictions shall be permitted (not applicable to check valves).

    Welding of pipe / pup pieces to welding end valves shall comply with MOG-EP-MET-STD-0012: MOTS-12 Welding and NDE of Welds.

    Plugs for drain and vent, etc., shall be of material not less noble than the valve body material.

    Threaded body connections shall be National Pipe Taper Thread (NPT), where the thread is protected by an O-ring above and below the thread. Refer to 13.6 Attachment 6: Drawing of Typical NPT Threaded Connection Detail for a typical NPT-threaded connection detail.

    The described solution, shall only apply for the sizes mentioned in the table below.

    ANSI Class Rating Valve nominal bore size

    150 >4 300 >4 600 >4 900 >4 1500 >2 2500 >2 4500 >2 9000 >2

    Table 8.1.1 Minimum valve size, where the threaded body solution shall apply

    Valves with hub ends shall be designed to allow mounting of clamps from manufacturer Grayloc, Techlok and G-Lok. The dimension of the clamps may differ between the three vendor types.

    The maximum force required to operate a valve under the maximum design pressure shall be 350N. Where a manual valve with standard operator requires force in excess 350N to operate, a gearbox shall be fitted.

  • This document contains proprietary information belonging to Maersk Oil and shall not be wholly or partially reproduced nor disclosed without prior written permission from Maersk Oil.

    MOG-EP-PIP-STD-0016 Rev 2.0

    Page 13 of 35

    Where required, the gearbox shall be sized such that the output torque shall be at least 1.5 times the maximum required operating torque of the valve.

    All exposed moving parts - e.g. spindles for gate valves which is non-coated due to its operating function, shall be covered by DENSO tape or equal to prevent corrosion while installed.

    8.1.1.1 Valve Signature

    The valve signature is required e.g. torque forces for horizontal hung actuators shall be part of the valve design. No bending forces into the connecting shaft shall be permitted.

    8.1.2 Ball Valves

    All top-entry valves shall be fully serviceable in the installed position without any pipe dismantling.

    Top-entry valves greater than 10 shall be delivered with necessary tools for dismantling of all valve internals, with the valve in the installed position.

    The ball support design shall comply with Table 8.1.2-1. Trunnion mounted valves may be offered in lieu of floating ball valves, but shall be clearly stated as a deviation to the request.

    Cavity bleed/vent connections shall be a threaded (NPT) plug where the thread is protected by an O-ring above and below the thread Refer to 13.6 Attachment 6: Drawing of Typical NPT Threaded Connection Detail.

    The lever or gear operator shall be part of the valve and supplied, together with the valve.

    Ball Valves: Floating Ball / Trunnion Mount

    ANSI pressure rating

    Valve size (NB)

    Reduced Bore

    Valve size (NB)

    Full Bore

    Floating Ball Trunnion

    Mount Floating Ball

    Trunnion

    Mount

    150# 1/2" 6" 8" 1/2" 4" 6

    300# 1/2" 6" 8 1/2" 4" 6

    600# 1/2" 6" 8 1/2" 4" 6

    900# 1/2" 4" 6 1/2" 3" 4

    1500# 1/2" 2" 3 1/2" 11/2" 2

    2500# 1/2" 2" 3 1/2" 11/2" 2

    4500# 1/2" 2" 3 1/2" 11/2" 2

    9000# 1/2" 2" 3 1/2" 11/2" 2

    Table 8.1.2-1 - Ball Valve Design

    The gear operator shall have a position indicator. The wrench or position indicator shall be in line with the pipeline when the valve is open and transverse when the valve is closed. The open and closed positions shall be clearly marked.

  • This document contains proprietary information belonging to Maersk Oil and shall not be wholly or partially reproduced nor disclosed without prior written permission from Maersk Oil.

    MOG-EP-PIP-STD-0016 Rev 2.0

    Page 14 of 35

    The lever length shall be less than twice the face-to-face length of the valve. The hand wheel diameter shall be less than 800mm.

    Gear operators needing more than 100 turns of the hand wheel for operation from fully open to fully closed shall not be permitted. The required number of turns to operate the valve shall be stated in the contract or PO.

    It shall not be possible for a leaking valve stem to cause pressurisation of the gearbox or actuator.

    Operator selection shall comply with Table 8.1.2-2, unless the maximum force/lever length combination specified above dictate that a gearbox shall be required.

    Ball Valves: Lever / Gear

    ANSI pressure rating

    Valve size (NB)

    Reduced Bore

    Valve size (NB)

    Full Bore

    Lever Gear Lever Gear

    150# 1/2" 6" 8" 1/2" 4" 6

    300# 1/2" 6" 8 1/2" 4" 6

    600# 1/2" 6" 8 1/2" 4" 6

    900# 1/2" 4" 6 1/2" 3" 4

    1500# 1/2" 4" 6 1/2" 3" 4

    2500# 1/2" 3" 4 1/2" 2" 3

    4500# 1/2" 2" 3 1/2" 1" 2

    9000# 1/2" 2" 3 1/2" 1" 2

    Table 8.1.2-2 - Ball Valve Operator Selection Guideline 8.1.3 Butterfly Valves

    Manual operated butterfly valves < 4 shall be delivered with a lever. Valves 4 shall be provided with a gear operator.

    8.1.4 Check Valves

    Wafer check valves for installation with flow vertical downwards shall have individually designed springs.

    8.1.5 Gate Valves

    Manually operated valves shall be provided with a gear operator as follows, unless specified otherwise in the contract or PO:

    Class 600 12 NPS and larger

    Class 900 10 NPS and larger

    Class 1500 6 NPS and larger

    Class 2500 4 NPS and larger

  • This document contains proprietary information belonging to Maersk Oil and shall not be wholly or partially reproduced nor disclosed without prior written permission from Maersk Oil.

    MOG-EP-PIP-STD-0016 Rev 2.0

    Page 15 of 35

    8.1.6 Globe Valves

    Manually operated valves shall be provided with a gear operator as follows, unless specified otherwise in the contract or PO:

    Class 150 8 NPS and larger

    Class 300 8 NPS and larger

    Class 600 6 NPS and larger

    Class 900 4 NPS and larger

    Class 1500 3 NPS and larger

    Class 2500 3 NPS and larger

    8.1.7 Needle Valves

    Needle valves shall have minimum 5mm (3/16) internal bore.

    Needle valves shall have an integral shoulder located below the packing, to prevent the needle from blow out. The shoulder shall not form part of the valve packing arrangement.

    The closure member shall be a two piece design to prevent rotation of the needle.

    The actuating thread shall be located above the valve packing.

    The closure member shall be designed such that a deformation of the handle, and stem just below handle, shall not affect the torque for operating the valve or shall be of sufficient robust design to prevent such deformation.

    The hand wheels/T-bars shall be operated without any use of tools at full differential pressure.

    When Carbon Steel (CS) is specified for the body, the needle valve assembly shall be AISI grade 316, 6% Mo Stainless Steel (SS), etc., but not AISI grade 304/308 or similar. When CRAs (AISI 316, 6% Mo SS, etc.) are specified for the body, the needle valve assemblies shall be of equally corrosion resistant material. Thus, for example, AISI 316 needle assembly in a 6% Mo SS body shall not be permitted.

    8.1.8 Slim-line Double Block and Bleed Valves

    Slim-line Double Block and Bleed Valves (SDBB) valves shall be used for instrument connections. Piping block valve in combination with instrument block and bleed valve shall not be used unless approved by BU TA-2.

    The primary isolation valve of SDBB valves shall be a bolted bonnet design needle valve, with minimum 4 bolts bolting the valve into the flange body.

    SDBB valves shall have minimum 5mm (3/16) internal bore.

    8.2 Actuators All control valves shall be provided with positioners to comply with MOG-EP-INS-STD-0001: MOTS-01 Instrument Materials and Installation for Instrument Materials and Installation (reference section 8.15.4, Positioners).

    Positioners shall be with integrated Current to Pneumatic Converter (I/P converter).

    Pneumatic positioners shall be supplied complete with regulator and gauges for input, output and air supply, integrally mounted.

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    MOG-EP-PIP-STD-0016 Rev 2.0

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    The control valve position control shall consist of the following:

    Air supply from the Instrument Air System with air filter and supply pressure regulator.

    Intelligent positioners with 4-20mA valve position control signal from the Supervisory Control and Data Acquisition (SCADA) system.

    Pneumatic output to the control valve.

    The air supply and the pneumatic output to the control valve shall each be provided with pressure indicator adjacent to the positioner.

    Positioners, filter regulators, filters, solenoid housings and the intelligent positioner units shall be in SS grade AISI 316. Weather resistant material shall be resistant to 100% humidity saturated with chlorides.

    Actuator and valves, including stem, seal system etc. shall be designed to allowing installation in any possible position.

    Actuator structural and energy containing components shall be constructed from CS and coated to comply with MOG-EP-MET-STD-0034: MOTS-34 Protective External Coating of Steel. The coating system shall be that suitable for machinery, equipment and panels with a surface temperature up to and including 120C.

    Actuators shall be fully supported on the valve. Requirement for external actuator support shall not be permitted.

    8.3 Actuated On/Off Valves (ESDV, BDV, XCV)

    Requirements for valve part shall be as specified on valve data sheet and this technical standard. The following requirements shall also apply.

    The actuator spring capacity and power stroke capacity shall be based on the required torque capacity multiplied by the safety factor in Table 8.3. The required torque capacity equals the maximum required torque during operation at full differential pressure multiplied with the safety factor, stated on the datasheet.

    Stem and stem-to-ball connection shall be designed for the maximum torque during valve operation by the higher of:

    Spring load or

    Specified maximum control media supply pressure.

    The safety factor against specified minimum yield strength of any part of the stem and stem-to-ball connection and all other drive train components shall be minimum 1.2 or the spring stroke torque requirement whichever the highest at the specified maximum regulated control media supply pressure.

    The value for maximum required torque to open/close valve shall be based on original documentation from the valve manufacturer.

    Emergency Shutdown Valve (ESDV) and Blowdown Valve (BDV) assembly shall be torque tested. Trust test shall apply for gate type ESDV and globe type BDV.

    BDVs

    At full differential design pressure, the valve shall be demonstrated to open by spring actuation.

    At full design pressure applied, the valve shall be demonstrated to close at minimum guaranteed control media supply pressure.

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    ESDVs

    At full design pressure applied at both ends, the valve shall be demonstrated to close by spring actuation

    At full differential design pressure, the valve shall be demonstrated to open at minimum guaranteed control media supply pressure.

    All opening and closing times (ESDVs and BDVs) shall be verified and recorded. Spring actuation times shall be controllable by adjustment of control media exhaust valve. The exhaust valve shall be fitted with a minimum stop or some other mechanism preventing it from being fully closed. The exhaust valve shall be fitted with a locking device to fix the valve in the set position.

    Minimum control media pressure to stay put shall be specified.

    The actuator mounting flange/bolting/materials shall be fully documented on a drawing. Any potential for galvanic corrosion between the actuator mounting flange on the valve and actuator supporting stool/flange shall be eliminated.

    The fail-safe position for ESDVs and BDVs shall be achieved by the use of spring return actuators.

    All actuated on/off valves shall be fitted with proximity type limit switches for both the open and closed position. In addition, they shall be fitted with visually readable position indicators for local indication.

    Solenoid valve, filter regulator and quick exhaust valve (if applicable) shall be made from SS grade AISI 316.

    The actuator torque safety factor specified in the data sheet shall be based on the values from Table 8.3.

    Bug screen shall be installed on solenoid valve air exhaust port and exhaust port in quick exhaust valve.

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    Actuator Torque Safety Factor

    ANSI Pressure Rating Valve Size ( bore ) Safety Factor

    150# 1/2" 12" 2.0

    14" 1.5

    300# 1/2" 8" 2.0

    10" 1.5

    600# 1/2" 8" 2.0

    10" 1.5

    900# 1/2" 6" 2.0

    8" 1.5

    1500#

    1/2" 4" 2.0

    6" 20" 1.5

    24" 1.5

    2500#

    1/2" 3" 2.0

    4" 14" 1.5

    16" 1.5

    4500# All 1.5

    9000# All 1.5

    Table 8.3 - Actuator Torque Safety Factor

    The Contractor shall complete and include the Actuator Torque Table, which forms part of the actuator data sheet found in 13.1 Attachment 1: Valve and Actuator Data Sheets, with their quotation for actuated valves.

    ESD and Riser valves shall be in accordance with section 8.4 Riser Valves.

    8.4 Riser Valves

    Requirements for valve part shall be as specified in valve data sheet and as specified for actuated on/off valves in this technical standard. Requirement for actuator part shall be as specified in actuator data sheet and as specified for actuators for actuated on/off valves in this technical standard. The following requirements shall also apply. Riser valves shall meet the requirements of ISO 14313/API 6D, ASME 16.34 or equivalent codes or standards including additional requirements specified in DNV-OS-F101. Valve with butt welding ends shall be delivered with one (or two as applicable) 1m long pup piece(s), manufactured from riser pipe material. The pup(s) shall be welded to the butt welding ends of the valve. External allowable loading of valve and pup piece and documentation hereof shall follow API 6D / ISO 14313: Pipeline Transportation Systems - Pipeline Valves, and other local additional requirements otherwise stated. Seat pockets, stem and trunnions sealing areas and body-to-bonnet sealing areas shall be overlaid with Inconel 625.

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    Valves that are welded into the pipeline shall be fully serviceable in the installed position. Valves that are welded into the pipeline shall be delivered with necessary tools for dismantling of all valve internals, with the valve in the installed position (welded), without any pipe dismantling. This includes but is not limited to retraction tools, supporting arrangements, seat retainers, etc. Alignment between body/bonnet shall be assured by sleeves inserted in minimum 4 boltholes. Accessories required to perform inline pipeline testing/cleaning with all valve internals removed shall be included in the delivery (blind flanges). During fabrication, valve shall be fully disassembled when pup piece is welded onto the valve body. Internal machining of the valve body shall be performed after the welding assembly of the valve components (body and pup piece). In case PWHT is not required and the welding assembly can be performed without impact on the required internal dimensions, the vendor can, on his own full responsibility, waive to the above requirement. In such case the vendor shall submit a full dimensional verification report for internal dimensions as part of the documentation. The assembly of the valve and the pup piece shall be in accordance with MOG-EP-MET-STD-0012: MOTS-12 Welding and NDE of Welds. Riser valves (ESDVs and XCVs) shall be fitted with body vents and sealant injection facilities to comply with Table 8.4. Riser ESDVs on high pressure systems shall be top entry, metal-to-metal seated, double piston type (sealing of platform side seat based on pressure from pipeline side) ball valves with coated ball and seats. Seat test shall be performed in compliance with EN 12266-1: Industrial Valves, Testing of Valves, Pressure Tests, Test Procedures and Acceptance Criteria - Mandatory Requirements, leakage rate B. The riser ESDV actuator shall be provided with a torque safety factor ratio of minimum 2.0. Riser XCVs in pipelines shall be fitted with a hard face coated ball. Applicable coating materials shall be UNS R30106 (e.g. STELLITE 6) or better (e.g. Tungsten Carbide), minimum hardness 39 HRC. The valve datasheet will state the required seat material.

    Seat sealant injection point Stem sealant

    injection point Cavity vent connection

    Riser ESDV (oil and water service) % - Prohibited

    Riser ESDV (gas service) % % - Prohibited Riser XCV (oil and water service) % - Prohibited Riser XCV (gas service) % - Prohibited

    Table 8.4 - Riser Valve Specification

    Sealant injection fittings shall be threaded (NPT) type. All sealant injection fittings shall incorporate two internal ball type non-return valves, a giant button head and a cover with vent holes that seals off the fitting by plugging the sealant port.

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    8.5 Control Valves (PCV, TCV, LCV, FCV, CVA)

    Requirements for control valves shall be as specified in data sheets. The following requirements shall also apply.

    Provisional size based on IEC 534-2: Industrial Process Control Valves Part 2-1: Flow Capacity shall be specified.

    For maximum flow at a given pressure drop, the calculated Valve Constant (CV) shall be approximately 80% for equal percentage and 90% for linear characteristic of the maximum CV for the selected valve. Final sizing shall be in accordance with valve manufacturer's formula and recommendation (including allowable turndown).

    Butterfly valves may be used as control valves for services where low-pressure drop with high capacity flow is required. Butterfly opening shall be limited to a maximum of 60 degrees. High performance (double or triple offset) type valves shall be used.

    Single seat valves shall have internal trim of the cage/seat ring retainer design, unless specified otherwise in the contract or PO. Where flashing or cavitation is anticipated, cage type shall be selected such that this effect is minimised.

    Angle valves shall be used for high-pressure drop applications (exceeding 70 barG) and where recommended by the manufacturer.

    Noise requirements shall be in accordance with MOG-EP-WEN-STD-0017: MOTS-17 Noise.

    Seat-leakage shall comply with FCI 70-2: Control Valve Seat Leakage, Class III minimum.

    For erosive/corrosive service, pressure drops above 15 bar or temperatures in excess of 300C, hard trim coating material shall be used. Hard trim coating materials include UNS R30106 (e.g. STELLITE 6) or better (tungsten carbide) protected trim, minimum hardness of 39 HRC, or 17-4 PH. 17-4 PH shall only be used if tempered after hardening at a temperature of minimum 550C. The heat treatment shall be documented.

    Non-standard bonnets (e.g. extended, finned, etc.) shall be used for continuous operating temperatures outside the limits -10C to +210C, and where standard bonnets may be covered by insulation, etc.

    The use of self-acting pressure regulators shall be limited to utility systems and a maximum regulated pressure of 10 barG, and where a variation in controlled pressure of 10% above or below the set point shall be permitted in the design system. Maximum valve size shall be limited to 4 NPS.

    8.6 Relief Valves

    Requirements shall be as specified in data sheets. The following requirements shall also apply.

    The basis for selection of pressure safety and relief devices shall comply with the requirements of API RP 520: Sizing, Selection and Installation of Pressure-Relieving Devices in Refineries, API RP 521; Guide for Pressure-Relieving and De-pressuring Systems, API STD 2000: Venting Atmospheric and Low-Pressure Storage Tanks, and ASME Section VIII Division 1: Rules for Construction of Pressure Vessels.

    Reference shall be made to the flare blow down and relief study for sizing of valves.

    When a backpressure of up to 10% of the setting may be expected, directly activated spring-loaded safety valves shall have balanced bellows. If continuous backpressure (liquid in discharge part) is present, the valve shall have bellows to isolate the process from the top work.

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    Pilot operated relief valves shall have a pressure test connection. The pressure pilot shall have a backflow preventer.

    Set pressure tolerances shall comply with ASME Section VIII Division 1, UG-126. Seat tightness shall comply with API STD 527: Seat Tightness of Pressure Relief Valves.

    For noise requirements see MOG-EP-WEN-STD-0017: MOTS-17 Noise.

    8.7 Control Panels

    Control systems shall be designed and built in compliance with schematics referred on actuator datasheets (listed in Table 8.7) and details for specific components listed on actuator datasheets.

    SS 316 panels shall be coated to comply with MOG-EP-MET-STD-0034: MOTS-34 Protective External Coating of Steel.

    The following schematics are available (included in section 13.5 Attachment 5: Valve Selection Manual.) Hydraulic Schematics (DK and UK)

    YYYY-08-01005-0001 Typical BDV/ESDV arrangement Type I ESD controlled

    YYYY-08-01005-0002 Typical BDV/ESDV arrangement Type II ESD and SCADA controlled

    YYYY-08-01005-0003 Typical ESDV arrangement Type III Only Svend and Roar

    YYYY-08-01005-0004 Typical ESDV arrangement Type VIII Quick exhaust

    YYYY-08-01006-0001 Typical XCV arrangement Type IV Stay put (upon hydraulic failure only)

    YYYY-08-01006-0002 Typical XCV arrangement Type V Fail open or close

    YYYY-08-01006-0003 Typical XCV arrangement Type VI Stay fixed

    YYYY-08-01006-0004 Typical XCV arrangement Type VII No signals to/from SCADA/ESD

    Pneumatic Schematics (DK)

    YYYY-08-01007-0001 Typical BDV/ESDV arrangement Type X Single SOV

    YYYY-08-01007-0002 Typical BDV/ESDV arrangement Type XI Single SOV with reset

    YYYY-08-01007-0003 Typical BDV/ESDV arrangement Type XII Double SOV

    Pneumatic Schematics (UK)

    YYYY-08-01009-0001 Typical BDV/ESDV arrangement Type X Single SOV

    YYYY-08-01009-0002 Typical BDV/ESDV arrangement Type XII Double SOV

    Pneumatic Schematics (Qatar)

    ASYYY-08-00200-0011 Typical BDV/ESDV arrangement Type X Single SOV

    ASYYY-08-00200-0012 Typical BDV/ESDV arrangement Type XI Single SOV with reset

    ASYYY-08-00200-0013 Typical BDV/ESDV arrangement Type X II Double SOV

    Table 8.7 - Control Panel Actuator Datasheet Guideline

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    9 Materials

    9.1 General

    All materials shall be in compliance with the Material Data Sheets in Appendix B. Table 9.1 identifies the testing and acceptance criteria for specific materials.

    Riser valves shall be submitted with 3.2 material certificates for the valve body and pup piece.

    MATERIAL TYPE

    MATERIAL DATA SHEET

    MD

    S1

    6 -

    CS

    -01

    MD

    S1

    6 -

    SS

    -01

    MD

    S1

    6 -

    SS

    -02

    MD

    S1

    6 -

    DS

    S-0

    1

    MD

    S1

    6 -

    DS

    S-0

    2

    MD

    S1

    6 -

    FC

    S-0

    1

    MD

    S1

    6 -

    FD

    SS

    -01

    Carbon Steel

    Forgings / Castings Austenitic Stainless Steel type 316/316L

    Forgings / Castings Austenitic Stainless Steel type 6% Mo

    Forgings / Castings Duplex Stainless Steel type 22% Cr

    Forgings / Castings Duplex Stainless Steel type 25% Cr

    Forgings / Castings Carbon Steel Fasteners

    Bolts / Nuts Duplex Stainless Steel type 25% Cr Fasteners

    Bolts / Nuts Table 9.1 - Materials Data Sheet Matrix

    Unless specified differently in the individual material data sheet, minimum test temperature shall be -46C for all CS material.

    For sub-size specimens, the reduction factor shall be the fractional sectional area equivalent to ASTM A370: Standard Test Methods and Definitions for Mechanical Testing of Steel Products, Table 9.

    9.1.1 Non-Destructive Examination

    In addition to requirements specified in the specific material data sheet, Non-Destructive Examination (NDE) shall be compulsory for all valves 2 in ASME 600# pressure system

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    and larger. NDE shall be performed and accepted in accordance with the design standard of the valve.

    9.1.2 Grease Nipple

    The standard grease nipple shall be of the same material as the valve body to avoid corrosion.

    9.2 Production Testing

    The Company reserves the right to perform chemical analysis and destructive testing on samples taken from the valve bodies and adaptors and to reject the complete set if test values do not comply with this technical standard, irrespective of the test bar results.

    9.3 Forged Valves

    9.3.1 General

    Forging shall be forged to or as close as possible to the final finished shape. Bar stock may be used for valve sizes 2 inches or less. Samples for testing shall be either sacrificial forging or extension test block that accurately represents the actual forging to be used.

    9.3.2 Carbon Steel

    Forged C-Mn steel material shall comply with MDS16-CS-01 Rev. 1 and as specified on the valve data sheet. The following additional/specific requirement shall be applicable:

    All valves shall meet the requirements of ISO 15156-2: Materials for Use in H2S-containing Environments in Oil and Gas Production, Annex A, SSC region 3.

    9.3.3 Austenitic Stainless Steel Type 316/316L

    Forged Austenitic SS type 316/316L material shall comply with MDS16-SS-01 Rev. 1 and as specified on the valve data sheet. The following additional/specific requirement shall be applicable:

    All pressure containing components shall undergo an Intergranular Corrosion (IGC) test in accordance with ASTM A262: Standard Practices for Detecting Susceptibility to Intergranular Attack in Austenitic Stainless Steels, practice E unless specified otherwise in the contract or PO.

    Stainless Steel shall not be permitted for temperatures above 60 C.

    9.3.4 Austenitic Stainless Steel Type 6% Mo

    Forged Austenitic SS type 6% Mo material shall comply with MDS16-SS-02 Rev. 1 and as specified on the valve data sheet. The following additional/specific requirement shall be applicable:

    All pressure containing components shall undergo a corrosion test in accordance with ASTM G48: Standard Test Methods for Pitting and Crevice Corrosion Resistance of Stainless Steels and Related Alloys by Use of Ferric Chloride Solutions, method A, and shall be documented. Test temperature shall be 50C and the exposure time 24 hours. The corrosion test specimen shall be at the same location as those for mechanical testing. Cut edges shall be prepared according to ASTM G48 and pickled (20% HNO3 + 5% HF, 60C, 5 minute).

    The acceptance criteria shall be:

    o No pitting at 20 times magnification.

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    MOG-EP-PIP-STD-0016 Rev 2.0

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    o The weight loss shall be less than 4.0 g/m2.

    9.3.5 Duplex Stainless Steel Type 22% Cr

    Forged Duplex SS type 22% Cr material shall comply with MDS16-DSS-01 Rev. 1 and as specified on the valve data sheet. The following additional/specific requirement shall be applicable: ASTM A923: Standard Test Methods for Detecting Detrimental Intermetallic Phase in Wrought Duplex Austenitic/Ferrite Stainless Steels, Test Method C, shall be performed and documented. The corrosion test specimen shall be extracted from at the same location as those for mechanical testing, unless specified otherwise in the contract or PO.

    9.3.6 Duplex Stainless Steel Type 25% Cr

    Forged Duplex SS type 25% Cr material shall comply with MDS16-DSS-02 Rev. 1 and as specified on the valve data sheet. The following additional/specific requirement shall be applicable:

    Corrosion test according to ASTM G48: Standard Test Methods for Pitting and Crevice Corrosion Resistance of Stainless Steels and Related Alloys by Use of Ferric Chloride Solutions, method A, shall be performed and documented. Test temperature shall be 50C and the exposure time 24 hours. The corrosion test specimen shall be at the same location as those for mechanical testing, unless specified otherwise in the contract or PO. Cut edges shall be prepared in accordance with ASTM G48 and pickled (20% HNO3 + 5% HF, 60C, 5 minute).

    The acceptance criteria shall be:

    o No pitting at 20 times magnification. o The weight loss shall be less than 4.0 g/m2.

    9.4 Cast Valves

    9.4.1 Representative Test Bar

    Samples for mechanical testing shall accurately represent the condition and properties in the actual components. Thickness of the test block shall be equal to the thickness of the actual components as heat treated, up to a maximum thickness of 100mm. For component thickness above 100mm, the test block thickness shall be at least 100mm. For flanged components, the largest flange thickness shall apply.

    Test specimens shall be cut from the 1/4T location from the surface, where T is the thickness of the test block.

    Test blocks shall be integrally cast with or grated onto the castings and shall not be removed from the castings until after the final quality heat treatment.

    Alternative test bar geometry shall not be permitted.

    9.4.2 Weld Repair

    Requirements shall be as specified in the relevant Material Data Sheets.

    9.4.3 Carbon Steel

    Cast C-Mn steel material shall comply with MDS16-CS-01 Rev. 1 and as specified on the valve data sheet.

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    9.4.4 Austenitic Stainless Steel Type 316/316L

    Cast Austenitic SS type 316/316L material shall comply with MDS16-SS-01 Rev. 1 and as specified on the valve data sheet. The following additional /specific requirement shall be applicable:

    All pressure containing components shall undergo a Strauss test in accordance with ASTM A262: Standard Practices for Detecting Susceptibility to Intergranular Attack in Austenitic Stainless Steels, practice E unless specified otherwise in the contract or PO.

    Stainless Steel shall not be permitted for temperatures above 60 C.

    9.4.5 Austenitic Stainless Steel Type 6% Mo

    Cast Austenitic SS type 6% Mo material shall comply with MDS16-SS-02 Rev. 1 and as specified on the valve data sheet. The following additional/specific requirements shall be applicable:

    Castings with Pitting Resistance Equivalent Number (PREN) 40 shall not be used for butt weld components, due to risk of micro cracking in the Heat Affected Zone (HAZ) in weldments.

    All pressure containing components shall undergo a corrosion test according to ASTM G48: Standard Test Methods for Pitting and Crevice Corrosion Resistance of Stainless Steels and Related Alloys by Use of Ferric Chloride Solutions, method A, and shall be documented. Test temperature shall be 50C and the exposure time 24 hours. The corrosion test specimen shall be extracted from at the same location as those for mechanical testing. Cut edges shall be prepared according to ASTM G48 and pickled (20% HNO3 + 5% HF, 60C, 5 minute).

    The acceptance criteria shall be:

    o No pitting at 20 times magnification. o The weight loss shall be less than 4.0 g/m2.

    9.4.6 Duplex Stainless Steel Type 22% Cr

    Cast Duplex SS 22% Cr material shall comply with MDS16-DSS-01 Rev. 1 and as specified on the valve data sheet. The following additional/specific requirements shall be applicable:

    Penetrant testing (S6) shall apply to all surfaces (including internal surfaces) of all castings. The examination shall be performed after final machining. Non-machined surfaces shall be pickled prior to the testing. The acceptance criteria shall be ASME Section VIII Division 1: Rules for Construction of Pressure Vessels, Appendix 7.

    The ASTM A923: Standard Test Methods for Detecting Detrimental Intermetallic Phase in Wrought Duplex Austenitic/Ferrite Stainless Steels, Test Method C, shall be performed and documented. The corrosion test specimen shall be extracted from the same location as those for mechanical testing.

    9.4.7 Duplex Stainless Steel Type 25% Cr

    Cast Duplex SS type 25% Cr material shall comply with MDS16-DSS-02 Rev. 1 and as specified on the valve data sheet. The following additional/specific requirements are applicable:

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    MOG-EP-PIP-STD-0016 Rev 2.0

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    Penetrant testing (S6) shall apply to all surfaces (including internal surfaces) of all castings. The examination shall be performed after final machining. Non-machined surfaces shall be pickled prior to the testing. The acceptance criteria shall be ASME Section VIII Division 1: Rules for Construction of Pressure Vessels, Appendix 7.

    Corrosion test shall be performed and documented in compliance with ASTM G48: Standard Test Methods for Pitting and Crevice Corrosion Resistance of Stainless Steels and Related Alloys by Use of Ferric Chloride Solutions, method A. Test temperature shall be 50C and the exposure time 24 hours. The corrosion test specimen shall be at the same location as those for mechanical testing. Cut edges shall be prepared according to ASTM G48 and pickled (20% HNO3 + 5% HF, 60C, 5 minute).

    The acceptance criteria shall be:

    o No pitting at 20 times magnification. o The weight loss shall be less than 4.0 g/m2.

    9.5 Modification

    Modification by welding shall be performed in compliance with MOG-EP-MET-STD-0012: MOTS-12 Welding and NDE of Welds and shall only be performed to a Company approved procedure. The welded area shall be examined 100% for internal and external defects. NDE performance, technique, acceptance, etc., shall be as specified by MOG-EP-MET-STD-0012.

    9.6 Valve Bolting

    Bolts and nuts for pressure-containing and pressure-controlling materials as well as attachment to valve body shall comply with the relevant valve specification and ASME B16.34: Valves Flanged, Threaded and Welding End. Threaded connections shall be added zinc oxide paste before assembling. (Zinc oxide paste: 1kg acid free oil mixed with 0.850kg zinc oxide).

    Pressure containing and controlling bolt, fasteners and nuts requirements;

    CS valves:

    o Shall be as specified in MDS16-FCS-01 Rev. 0 SS valves:

    o Shall be as specified in MDS16-FDSS-01 Rev. 0 o Age/precipitation hardened bar shall not be used for fabrication of bolts.

    Nickel Aluminium Bronze valves:

    o Shall be as specified in MDS16-FDSS-01 Rev. 0 o Age/precipitation hardened bar shall not be used for fabrication of bolts.

    General requirements;

    Surface Treatment for CS Bolts and nuts;

    o Sizes M12 or " or larger shall be hot dip galvanized according to ASTM A153: Standard Specification for Zinc Coating (Hot-Dip) on Iron and Steel Hardware or ISO 1461: Metallic Coatings - Hot Dip Galvanized Coatings on Fabricated Iron and Steel Articles - Specifications and Test Methods. Sizes up to M12 or ", zinc electroplate according to ASTM B633: Standard Specification for Electrodeposited Coatings of Zinc on Iron and

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    Steel, class Fe/Zn 12 with type II finish (colour chromate conversion coating).

    All non-pressure retaining and internal bolts and nuts shall be homogenous with the valve material and fit for purpose.

    9.7 Gaskets, Seals and Packing Materials

    Asbestos containing material shall not be used.

    Graphite based gaskets, seals and packing materials shall not be used in sea water service.

    All gaskets, seals and packing materials shall be suitable for the service conditions specified on the data sheets.

    Seals shall be Anti-Explosive Decompression resistant (AED) in design and material. AED elastomer seals shall not be thicker than 6 mm.

    9.8 Actuator Bolting

    Actuator bolting and tie rod material shall be of a quality and strength equivalent to grade B7 of ASTM A193: Standard Specification for Alloy-Steel and Stainless Steel Bolting Materials for High Temperature or High Pressure Service and Other Special Purpose Applications.

    Nuts shall be of a quality and strength corresponding to grade 2H of ASTM A194: Standard Specification for Carbon and Alloy Steel Nuts for Bolts for High Pressure or High Temperature Service, or Both.

    Actuator bolting shall be hot dip galvanised and centrifuged and coated to comply with MOG-EP-MET-STD-0034: MOTS-34 Protective External Coating of Steel. The coating system shall be that suitable for machinery, equipment and panels with a surface temperature up to and including 120C.

    10 General Requirements

    This section specifies the general requirements for packing, preservation and storage/handling.

    10.1 Pressure Testing

    Pressure test requirements shall be in accordance with the design standard.

    Other requirements shall be;

    Internally coated or lined valves shall be shell tested before and after application of coating or lining. This requirement doesnt apply to weld overlaid valves.

    After testing with water, all valves shall be thoroughly cleaned and dried to prevent possible corrosion from the water.

    All pressure tests shall be repeated on valves after any weld repair to the pressure retaining components.

    If the drain/vent plug is removed during seat tightness test, tightness of the plug to be revalidated by a separate pneumatic test at the end of the test sequence.

  • This document contains proprietary information belonging to Maersk Oil and shall not be wholly or partially reproduced nor disclosed without prior written permission from Maersk Oil.

    MOG-EP-PIP-STD-0016 Rev 2.0

    Page 28 of 35

    10.2 Painting

    All steel surfaces exposed to the environment (valve, actuator, transition pieces, etc.) shall be painted in compliance with MOG-EP-MET-STD-0034: MOTS-34 Protective External Coating of Steel.

    Nameplates and other attachments shall be mounted AFTER the final coating layer has been applied.

    10.3 Pickling and Passivation

    SS valves shall be pickled and passivized to restore the surface after welding or after any surface contamination, e.g. grinding dust, etc.

    Deliveries shall be packed and preserved, allowing for onshore and offshore storage and handling.

    All machined surfaces shall be coated with grease-based corrosion protection.

    Valve ends shall be covered with close fitting wooden caps to protect the machined parts and prevent ingress of foreign bodies, dirt or moisture.

    If packing includes the inclusion of a desiccant material inside the valve, this shall be identified on the end protector or on a tag securely fastened to the valve.

    If storage is performed at vendors premises, all machined surfaces shall be inspected on a regular basis.

    Packing shall allow for a means to be safely handled onshore and offshore.

    11 Certification

    Certification shall comply with requirements outlined on data sheets and specified below. Upon delivery of valve(s), valve supplier shall upgrade the Company approved valve data sheet to AS-BUILT status. The included statement of compliance shall be stamped and duly signed.

    Valves shall be documented (and CE marked where applicable) in compliance with 97/23/EC: Directive of the European Parliament and of the Council on the Approximation of the Laws of the Member States Concerning Pressure Equipment (PED) - Classification according to Diagram 6, Annex II and 98/37/EC: Machinery Safety Directive, when delivered to EU.

    ATEX applicable components for actuated valves shall be documented with a Declaration of Conformity and marking to comply with ATEX 94/9/EC: Atmospheric Explosive Directive. Equipment and Protective Systems Intended for Use in Potentially Explosive Atmospheres, based on Equipment Group II, Equipment Category 2, when delivered to EU.

    Third party release note covering design approval, approval of welding procedures and survey during fabrication shall be required for all Certification Class 1 valves. The release note shall state that the valves have been designed, fabricated, tested, inspected and found to comply with Company technical standards.

    Third party release note for review of documentation shall be required for all Certification Class 2 valves. The release note shall state that the valves have been designed, fabricated, tested, inspected and found to comply with Company technical standards.

    Third party involvement shall not be required for Certification Class 3 valves.

    The following valve Certification Class definitions shall be applied:

    Class 1 valves: All valves of welded construction, with a rating of 600# and above, and all riser ESDVs.

  • This document contains proprietary information belonging to Maersk Oil and shall not be wholly or partially reproduced nor disclosed without prior written permission from Maersk Oil.

    MOG-EP-PIP-STD-0016 Rev 2.0

    Page 29 of 35

    Class 2 valves: All valves of welded construction, with a rating of 300# and below.

    Class 3 valves: Other valves.

    12 Documentation

    Documentation shall comply with Company Documentation requirements outlined on the datasheets.

    As built updated G.A. drawings of valve and sub components shall be part of the final documentation.

    12.1 Drawings

    Vendor shall as part of the order clarification provides detailed drawings of the weld overlay and pocket areas. Detailed G.A. Drawings of the valve and subcomponents shall be part of the clarification process.

    12.2 Riser Valves

    Vendor shall as part of the RFQ process provide detailed drawings of the full assembly, including the actuator and the connection piece in-between.

    13 Attachments

    The following attachments are only provided in the electronic version.

    13.1 Attachment 1: Valve and Actuator Data Sheets

    Datasheets for the following valve types are included in the electronic version.

    13.1.1 Actuators

    Standard actuator datasheet and actuator torque table are included in the electronic version.

    13.1.2 Control Valves

    Standard actuator datasheet and actuator torque table are included in the electronic version.

    13.1.3 Pressure Safety Valves

    Standard Pressure Safety Valve (PSV) datasheet is included in the electronic version.

    13.2 Attachment 2: Control Diagrams

    Included in the electronic version:

    Hydraulic Schematics (DK and UK)

    I. YYYY-08-01005-0001

    II. YYYY-08-01005-0002 III. YYYY-08-01005-0003 IV. YYYY-08-01005-0004 V. YYYY-08-01006-0001

    VI. YYYY-08-01006-0002

  • This document contains proprietary information belonging to Maersk Oil and shall not be wholly or partially reproduced nor disclosed without prior written permission from Maersk Oil.

    MOG-EP-PIP-STD-0016 Rev 2.0

    Page 30 of 35

    VII. YYYY-08-01006-0003 VIII. YYYY-08-01006-0004

    Pneumatic Schematics (DK)

    X. YYYY-08-01007-0001

    XI. YYYY-08-01007-0002 XII. YYYY-08-01007-0003

    Pneumatic Schematics (UK)

    X. YYYY-08-01009-0001

    XII. YYYY-08-01009-0002

    Pneumatic Schematics (Qatar)

    X. ASYYY-08-00200-0011

    XI. ASYYY-08-00200-0012 XII. ASYYY-08-00200-0013

    13.3 Attachment 3: Piping Specification

    Included in the electronic version.

    13.4 Attachment 4: Valve Specification

    Included in the electronic version.

    13.5 Attachment 5: Valve Selection Manual

    Included in the electronic version.

    13.6 Attachment 6: Drawing of Typical NPT Threaded Connection Detail

    Included in the electronic version.

    14 Appendices

    Appendix A BU Country Specific Requirements Appendix B Material Data Sheet for Forgings and Castings

  • This document contains proprietary information belonging to Maersk Oil and shall not be wholly or partially reproduced nor disclosed without prior written permission from Maersk Oil.

    MOG-EP-PIP-STD-0016 Rev 2.0

    Access to Attachment 1: Valve and Actuator Data Sheets For access to Attachment 1: Valve and Actuator Data Sheets please follow this link: MOTS-16 Valves Rev. 2.0 Attachment 1 Valve and Actuator Data Sheets

  • This document contains proprietary information belonging to Maersk Oil and shall not be wholly or partially reproduced nor disclosed without prior written permission from Maersk Oil.

    MOG-EP-PIP-STD-0016 Rev 2.0

    Access to Attachment 2: Types of Control Panels For access to Attachment 2: Types of Control Panels please follow this link: MOTS-16 Valves Rev. 2.0 Attachment 2 Types of Control Panels

  • Attachment 3

    PIPING SPECIFICATION

    Piping Denomination Code

    1st Letter:

    A = 150 lb ANSI Pressure Class Rating

    B = 300 lb ANSI Pressure Class Rating

    D = 600 lb ANSI Pressure Class Rating

    E = 900 lb ANSI Pressure Class Rating

    F = 1500 lb ANSI Pressure Class Rating

    G = 2500 lb ANSI Pressure Class Rating

    H = 9000 lb special Pressure Class Rating

    J = 4500 lb special Pressure Class Rating

    2nd Letter

    D = Carbon, Low Temp. - Sour Process and Utility

    E = Carbon, Low Temp. - Sour Process and Utility

    F = Carbon, Low Temp. - Sour Process and Utility

    G = Galvanized CS, Utility System Galvanized

    H = PVDF, Sodium Hypochlorite

    J = ELASTOPIPE, Sea Water and Fire Water

    K = CUNIFER, Seawater

    M = SS (6% Mo), Sour Process and Sea Water

    N = SS (6% Mo), Sea Water and Fire Water

    O = Super Duplex, Sour process and utility

    P = PE, Sea Water, Potable Water

    R = GRE, Sewage Water, Open Drains, Potable Water

    S = SS, Low Temp., Sour Process and Utility

    T = Titanium, Ferric Chlorite, Sodium Hypochlorite

    U = Copper, Domestic Hot and Cold Water

    X = Duplex, Sour Process and Utility

    Y = Material not covered by piping specifications

    Z = Carbon, Low Temp. - Sour Process and Utility

    3rd Letter

    M = Modified (e.g. pressure, material etc.) version of piping specification to suit special purposes

    3rd or 4th Letter

    W = Intended for water injection service, ref. section 7.3 for requirements

  • Attachment 3

    PIPING SPECIFICATION INDEX

    Spec No.

    Rev. Rating Test Pressure (Psig)

    Service Corrosion Allowance (mm)

    Material

    AD 1 150 RF 428 Low Temp. Sour Process 3.0 LTCS AG 1 150 FF 338 Utility Systems Galvanized 1.3 CS(Galv.) AH 1 150 RF 113 Sodium Hypochlorite Nil PVDF AJ 0 150 RF 435 Sea Water/Fire Water Deluge Dry Nil ELASTOPIPE AK 1 150 FF 338 Sea Water Nil Cu/Ni AM 1 150 RF 435 Sour Process & Utility, Seawater Nil SS (6% Mo)

    AMM 1 150 RF 435 Sour Process & Utility Nil SS (6% Mo) AN 1 150 RF 435 Sea Water & Fire Water Nil SS (6% Mo) AO 1 150 RF 435 Sour Process & Utility Nil Super Dupl. AP 1 150 FF 218 Sea Water, Potable Water for Accom. Nil PE AR 0 150 FF&RF 346 Sewage Water, Open Drains, Pot.Water Nil GRE AS 1 150 RF 345 Low Temp. Sour Process & Utility Nil SS AT 0 150 RF 345 Ferric Chl., Sodium Hypochlorite Nil Titanium AU 1 150 RF 218 Domestic Hot & Cold Water Nil Copper AX 1 150 RF 435 Sour Process & Utility Nil SS (Duplex) AZ 1 150 RF 428 Sour Process & Utility Drain 6.0 LTCS BD 1 300 RF 1110 Low Temp. Sour Process & Utility 3.0 LTCS BG 1 300 FF 750 Utility Systems Galvanized 1.3 CS(Galv.) BM 1 300 RF 1125 Sea Water, Sour Process Nil SS (6% Mo) BO 1 300 RF 1125 Sour Process & Utility Nil Super Dupl. BS 1 300 RF 900 Low Temp. Sour Process & Utility Nil SS BX 1 300 RF 1125 Sour Process & Utility Nil SS (Duplex) BZ 1 300 RF 1110 Sour Process & Utility Drain 6.0 LTCS DD 1 600 RTJ 2220 Low Temp. Sour Process & Utility 3.0 LTCS DM 1 600 RTJ 2250 Sour Process & Utility Nil SS (6% Mo) DO 1 600 RTJ 2250 Sour Process & Utility Nil Super Dupl. DS 0 600 RTJ 1800 Low Temp. Sour Process & Utility Nil SS DX 0 600 RTJ 2250 Sour Process & Utility Nil SS (Duplex) DZ 1 600 RTJ 2220 Sour Process & Utility Drain 6.0 LTCS ED 1 900 RTJ 3330 Low Temp. Sour Process & Utility 3.0 LTCS EM 1 900 RTJ 3375 Sour Process & Utility Nil SS (6% Mo) EO 1 900 RTJ 3375 Sour Process & Utility Nil Super Dupl.

    ES 0 900 RTJ 2700 Low Temp. Sour Process & Utility Nil SS

    ESM 0 900 RTJ 3240 Low Temp. Sour Process & Utility Nil SS

    EX 1 900 RTJ 3375 Sour process & Utility Nil SS (Duplex) FD 1 1500 RTJ 4950 Low Temp. Sour Process & Utility 3.0 LTCS FE 1 1500 RTJ 5558 Low Temp. Sour Process & Utility 3.0 LTCS FO 1 1500 RTJ 5625 Sour process & utility Nil Super Dupl.

    FS 0 1500 RTJ 4500 Low Temp. Sour Process & Utility Nil SS

    FX 1 1500 RTJ 5625 Sour Process & Utility Nil SS (Duplex) GD 1 2500 RTJ 5700 Low Temp. Sour Process & Utility 3.0 LTCS GE 1 2500 RTJ 6750 Low Temp. Sour Process & Utility 3.0 LTCS GF 1 2500 RTJ 7800 Low Temp. Sour Process & Utility. 3.0 LTCS

    GFM 1 2500 RTJ 7800 Low Temp. Sour Process & Utility 3.0 LTCS/API GO 1 2500 RTJ 7005 Sour process & utility Nil Super Dupl.

    GS 0 2500 RTJ 7500 Low Temp. Sour Process & Utility Nil SS

    GX 0 2500 RTJ 6750 Sour process & utility Nil Super Dupl.

    HA 1 9000 Special 13500 Sweet Process & Utility 1.3 CS

    HO 1 9000 Special 13500 Sour Process & Utility Nil Super Dupl.

    JM 2 4500 Special 16875 Sour Process & Utility Nil SS (6% Mo)

    JO 1 4500 Special 16875 Sour Process & Utility Nil Super Dupl.

  • Attachment 4

    VALVES SPECIFICATION Valve Denomination Code

    Example: ( ) V BA 6 G R (1) * * * * * * ** Service Code * * * * * * * * * * * ******** Special Identifier where required * * * * * * * * * *************** Type of Connection * * * * * * * ********************* Type of Valve * * * * * *************************** Piping Specification * * * ********************************** V for Valve * *************************************** Nominal Valve Size Type Valve 1 - SDBB (Slim-line Double Block and Bleed) 2 - Gate 3 - Globe 4 - Duo-Check 5 - Plug 6 - Ball 7 - Swing, Ball and Piston Check 8 - Butterfly 9 - Instrument Needle Valve Type Connection BW - Butt Weld BW/S - Inlet Butt Weld/Outlet Screwed (NPT thread only) C - Capillary F - Flanged FSW - Fusion Socket Weld, thermal G - Grayloc G/S - Inlet Grayloc/Outlet Screwed (NPT thread only) S - Screwed (NPT thread only) SW - Socket Weld SW/S - Inlet Socket Weld/Outlet Screwed (NPT thread only) T - Taperlok W - Wafer Special Identifier (F) - Full Bore (R) - Reduced Bore Service Code

    1 General 2 Gas - general 3 Gas - high temperature 4 Process with sand 5 WI

  • Attachment 5 - Valve Selection Manual

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    Service Code 1; General ServiceProcess BV SS GBV/BV SS CV GBV GBVSeawater BUV/VRP*1 BV SS CV BUV/VRP*1 Firewater BUV BV SS CV GBVOther utility BV SS GBV/BV SS CV GBV

    Service Code 2; Gas - General Service BV SS GTV GBV/BV SS CV GBV GBV

    Service Code 3; Gas - High Temp 2500# BV MS GTV GBV/BV MS CV AS CV GBV GBV1500# and below BV SS GTV GBV/BV SS CV AS CV GBV GBV

    Service Code 4; Process with sandProcess lines upstream 1st stage separator PV BV MS GTV GBV/BV MS CV GBV CHVProduced water lines where sand is expected PV BV MS GTV GBV/BV MS CV GBV CHV

    Service Code 5; Water Injection BV SS PV GTV GBV/BV SS CV AS CV GBV CHV

    Valve Type DesignationsBall Valve soft seated BV SS Note 1 When rubber spool Pinching is selected project specific datasheet shall be made and approved Ball Valve metal seated BV MS by CompanyPlug Valve PVGate Valve GTVGlobe Valve GBVButterfly Valve BUVCheck Valve CV Valve type shall be selected in the order of priority indicated. If lower priority valve type is selected,Check Valve Anti Slam CV AS contractor shall submit written argumentation, and obtain Company's written approval.Rubber Spool Pinching VRPChoke Valve CHV

    Service Code. (Ref Section 6)

    BDVHCV/XCV/ESDV Check Valves Control Valves - High DPValve Function

    Control Valves

  • This document contains proprietary information belonging to Maersk Oil and shall not be wholly or partially reproduced nor disclosed without prior written permission from Maersk Oil.

    MOG-EP-PIP-STD-0016 Rev 2.0

    Page 31 of 35

    Appendix A BU Country Specific Requirements A1 Maersk Oil Denmark (MODK) Requirements

    A.1.1 Riser Valves

    For any deviations between DBU technical specification for riser ESDVs and section 8.4, Riser valves for DBU shall be in accordance with DBU technical specification for riser ESDVs when applicable.

    A.1.2 Documentation

    Documentation shall comply with Company Documentation Standard A-05 Certification Dossier and the requirements outlined on the datasheets.

    A2 - Maersk Oil U.K. (MOUK) Requirements

    A.2.1 Scope

    It should be noted that this technical standard has been developed from the equivalent MOG Technical Standard and contains references/information that may not be applicable to the UK. In these cases, the existing local specifications (i.e. classes, valve data sheets, piping specials, etc.) are to be adopted until such time that the MOG to MONS piping class conversion process has been completed.

    A.2.2 Mandatory Regulations

    Pressure Equipment Regulations SI 1999/2001 (PER)*

    Offshore Installations (Safety Case) Regulations (SCR) 2005 SI 3117:2005

    Offshore Installations (Design and Construction) Regulations (DCR), SI 913: 1996.

    Offshore Installations (Prevention of Fire and Explosion, and Emergency Response) Regulations (PFEER), SI 743: 1995

    * The Pressure Equipment Directive is implemented in the UK as the Pressure Equipment Regulations (PER): 1999, (SI 1999 No. 2001) which stipulates the legislative requirements.

    A.2.3 Codes and Standards

    Pipelines within the UK sector are required to be in accordance with the following:

    EN 14161 Pipeline Transportation Systems

    PD 8010 Code of Practice for Pipelines

    A2.4 Specification

    It should be noted that this technical standard has been developed from the equivalent MOG Technical Standard and contains references/information that may not be applicable to the UK. In these cases, the existing local specifications (i.e. classes, valve data sheets, piping specials, etc.) are to be adopted until such time that the MOG to MONS piping class conversion process has been completed.

  • This document contains proprietary information belonging to Maersk Oil and shall not be wholly or partially reproduced nor disclosed without prior written permission from Maersk Oil.

    MOG-EP-PIP-STD-0016 Rev 2.0

    Page 32 of 35

    A3 - Maersk Oil Qatar (MOQ) Requirements

    A.3.1 Mandatory Regulations

    Although not mandatory for the Qatar operating region, the requirements of EC Directive 97/23/EC (Pressure Equipment) and EC Directive 98/37/EC (Machinery) have been adopted by Maersk Oil Qatar and full compliance is required. In the event that the Seller can demonstrate and offer a commercial saving to Maersk Oil Qatar greater than 5% of the unit item cost by not complying with these regulations, the Seller may offer