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API Std 520, Part 2 Sizing, Selection, and Installation of Pressure-relieving Devices-Part II, Installation, Sixth Edition

standard by American Petroleum Institute, 03/01/2015

Full Description

Please note that any addenda or errata may not be included in translated editions of this standard.

This standard covers methods of installation for pressure-relief devices (PRDs) for equipment that has a maximum allowable working pressure (MAWP) of 15 psig (1.03 barg or 103 kPAg) or greater.

Pressure-relief valves (PRVs) or rupture disks (RDs) may be used independently or in combination with each other to provide the required protection against excessive pressure accumulation.

As used in this standard, the term pressure-relief valve includes safety relief valves used in either compressible or incompressible fluid service, and relief valves used in incompressible fluid service.This standard covers gas, vapor, steam, two-phase, and incompressible fluid service; it does not cover special applications that require unusual installation considerations.

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520 Part 2 e6 pages.fm


Sizing, Selection, and Installation of Pressure-relieving Devices

Part II—Installation


API STANDARD 520

SIXTH EDITION, MARCH 2015




Special Notes


API publications necessarily address problems of a general nature. With respect to particular circumstances, local, state, and federal laws and regulations should be reviewed.


Neither API nor any of API’s employees, subcontractors, consultants, committees, or other assignees make any warranty or representation, either express or implied, with respect to the accuracy, completeness, or usefulness of the information contained herein, or assume any liability or responsibility for any use, or the results of such use, of any information or process disclosed in this publication. Neither API nor any of API's employees, subcontractors, consultants, or other assignees represent that use of this publication would not infringe upon privately owned rights.


API publications may be used by anyone desiring to do so. Every effort has been made by the Institute to assure the accuracy and reliability of the data contained in them; however, the Institute makes no representation, warranty, or guarantee in connection with this publication and hereby expressly disclaims any liability or responsibility for loss or damage resulting from its use or for the violation of any authorities having jurisdiction with which this publication may conflict.


API publications are published to facilitate the broad availability of proven, sound engineering and operating practices. These publications are not intended to obviate the need for applying sound engineering judgment regarding when and where these publications should be utilized. The formulation and publication of API publications is not intended in any way to inhibit anyone from using any other practices.


Any manufacturer marking equipment or materials in conformance with the marking requirements of an API standard is solely responsible for complying with all the applicable requirements of that standard. API does not represent, warrant, or guarantee that such products do in fact conform to the applicable API standard.


Users of this Standard should not rely exclusively on the information contained in this document. Sound business, scientific, engineering, and safety judgment should be used in employing the information contained herein.


Work sites and equipment operations may differ. Users are solely responsible for assessing their specific equipment and premises in determining the appropriateness of applying the Standard. At all times users should employ sound business, scientific, engineering, and judgment safety when using this Standard.


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Copyright © 2015 American Petroleum Institute


Foreword


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Suggested revisions are invited and should be submitted to the Standards Department, API, 1220 L Street, NW, Washington, DC 20005, standards@api.org.


  1. Scope 1

  2. Normative References 1

  3. Terms and Definitions 1

  4. PRD Location 1

    1. General 1

    2. Proximity to Protected Equipment 1

    3. Pressure Fluctuations 1

    4. Vibration 2

    5. Operating Environment 3

    6. Free-draining 3

    7. Maintainability 3

  5. Inlet Piping Requirements 3

    1. General 3

    2. Minimum Diameter 4

    3. Layout 4

    4. Isolation Valves in Inlet Piping 6

    5. Process Laterals Connected to Inlet Piping of PRVs 6

    6. PRV Inlet Line Length and Pressure Loss 6

    7. Inlet Stresses that Originate from Static Loads in the Discharge Piping 7

    8. Inlet Stresses that Originate from Discharge Reaction Forces 7

  6. Discharge Piping 10

    1. General 10

    2. Safe Disposal of Relieving Fluids 10

    3. Backpressure Limitations and Sizing of Pipe 10

    4. Considerations for Pilot-Operated PRVs 11

    5. Stresses in Discharge Piping During Release 11

    6. Isolation Valves in the Discharge Piping 11

    7. Rupture Disks Installed at the Outlet of a PRV 11

  7. PRV Stability 12

    1. General 12

    2. Potential Causes of PRV Instability 13

    3. PRV Inlet Pressure Drop Limitations 14

    4. PRV Trim Selection 22

8P RD Isolation (Stop) Valves 22

    1. General 22

    2. Application 22

    3. Isolation Valve Requirements 22

    4. Examples of Isolation Valve Installations 30

    5. Administrative Controls Related to Isolation Valves 31

Contents

Page

  1. Rupture Disk Installations 32

    1. Rupture Disk Devices in Combination with PRVs 32

    2. Rupture Disks In Series 34

  2. Bonnet or Pilot Vent Piping 34

    1. General 34

    2. Conventional Valves 34

    3. Balanced Bellows Valves 34

    4. Balanced Piston Valves 39

    5. Pilot-Operated Valves 39

  3. Drain Piping 39

    1. Installation Conditions that Require Drain Piping 39

    2. Safe Practice for Installation of Drain Piping 39

  4. Pre-installation Handling and Inspection 39

    1. General 39

    2. Storage and Handling of PRDs 40

    3. Inspection and Cleaning of Systems Before Installation 40

  5. Pressure-relief Device Installation and Maintenance 40

    1. Mounting Position 40

    2. Care in Installation 40

    3. PRVs 40

    4. Rupture Disk Devices 41

    5. Pin-actuated Devices 41

    6. Proper Gasketing and Bolting for Service Requirements 41

    7. Inspection and Maintenance 41

    8. Test or Lifting Levers 41

    9. Heat Tracing and Insulation 42

Annex A (informative) Rupture Disk Installation Guidelines 43

Annex B (informative) Installation and Maintenance of Pin-actuated Non-reclosing PRDs 49

Annex C (informative) PRV Acoustic Interaction 51

Bibliography 54


Figures

  1. Typical Installation Avoiding Unstable Flow Patterns at PRV Inlet 2

  2. Typical Pressure-relief Valve Installation: Atmospheric (Open) Discharge 3

  3. Typical Pressure-relief Valve Installation: Closed System Discharge 4

4A Typical Rupture Disk Device Installation: Atmospheric (Open) Discharge 5

4B Typical Rupture Disk Device Installation: Atmospheric (Open) Discharge 5

  1. Avoiding Process Laterals Connected to Pressure-relief Valve Inlet Piping 6

  2. Typical Pressure-relief Valve Installation with Vent Pipe 8

  3. Typical Pressure-relief Valve Mounted on Process Line 18

  4. Typical Pressure-relief Valve Mounted on Long Inlet Pipe 19

  5. Typical Pilot-Operated Pressure-relief Valve Installation 21


  6. Typical PRD Installation with an Isolation Valve 25

  7. Typical PRD Installation for 100 % Spare Relieving Capacity 26

  8. Alternate PRD Arrangement for 100 % Spare Relieving Capacity 27

  9. Alternate PRD Installation Arrangement for 100 % Spare Relieving Capacity 28

  10. Three-Way Changeover Valve—Shuttle Type 29

  11. Three-Way Changeover Valve—Rotor Type 29

  12. Three-Way Changeover Valve—Ball Types 30

  13. Typical Flare Header Block Valves 31

  14. Typical Isolation Block Valves for Spare Compressor 32

  15. Typical Rupture Disk Device in Combination With Relief Valve: Inlet Side Installation 33

  16. Bonnet Vent for Bellows Valves with Vent Located at the PRV 35

  17. Bonnet Vent for Bellows Valves Handling Vapor with Remote Vent Location 36

  18. Bonnet Vent for Bellows Valves Handling Liquids Where a Leak Needs to Be Routed Away

    from the PRV 37

  19. Bonnet Vent for Bellows Valves Handling Liquids or Flashing Liquid and Vapor with Remote

Vent Location 38

    1. Typical Configuration of Companion Flanges, Gaskets and Rupture Disk Assembly 44

    2. Proper Handling of a Rupture Disk 46

    3. Improper Handling of a Rupture Disk 46

    4. Proper Alignment of Rupture Disk indicated by Tag Arrows 47


Tables

  1. Performance Differences with PRV Trim 23

  2. Design Guidance for PRV Trim Options 23


vii


Sizing, Selection, and Installation of Pressure-relieving Devices Part II—Installation


  1. Scope

    This standard covers methods of installation for pressure-relief devices (PRDs) for equipment that has a maximum allowable working pressure (MAWP) of 15 psig (1.03 barg or 103 kPAg) or greater. Pressure-relief valves (PRVs) or rupture disks (RDs) may be used independently or in combination with each other to provide the required protection against excessive pressure accumulation. As used in this standard, the term pressure-relief valve includes safety- relief valves used in either compressible or incompressible fluid service, and relief valves used in incompressible fluid service. This standard covers gas, vapor, steam, two-phase, and incompressible fluid service; it does not cover special applications that require unusual installation considerations.


  2. Normative References

    The following referenced documents are indispensable for the application of this document. For dated references, only the edition cited applies. For undated references, the latest edition of the referenced document (including any amendments) applies.


    API Standard 520, Sizing, Selection, and Installation of Pressure-relieving Devices, Part I–Sizing and Selection


  3. Terms and Definitions

    The terminology for PRDs that is used in this standard is in general agreement with the definitions given in API 520 Part I.


  4. PRD Location

    1. General


      There are a number of design factors that should be considered when determining the location of the PRD.


    2. Proximity to Protected Equipment


      If other factors permit, the PRD should normally be placed close to the protected equipment or system of equipment so that the pressure in the protected equipment stays within Code allowable limits and to avoid PRV instability (see Section 7).


      See 7.3.3 for guidance on establishing set pressure if PRD will be remote from the protected equipment.


    3. Pressure Fluctuations


The PRD should not be located where there are pressure fluctuations large enough to result in relief valve simmering/ activation or rupture disk fatigue. On installations that have pressure fluctuations that peak close to the set pressure of the PRV or burst pressure of a rupture disk, the PRD should be located farther from the source and in a more stable pressure region.


Examples of areas that may have pressure fluctuations include:


  • locations close to control valves, other valves, and other appurtenances;


  • locations close to orifice plates and flow nozzles;

1