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API RP 576

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API RP 576 Inspection of Pressure Relieving Devices

standard by American Petroleum Institute, 12/01/2000

Full Description

This recommended practice describes the inspection andrepair practices for automatic pressure-relieving devices commonlyused in the oil and petrochemical industries. As aguide to the inspection and repair of these devices in theuser's plant, it is intended to ensure their proper performance.This publication covers such automatic devices as pressurerelief valves, pilot-operated pressure relief valves, rupturedisks, and weight-loaded pressure vacuum vents.

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RP 576


Inspection of

Pressure-Relieving Devices


API RECOMMENDED PRACTICE 576 SECOND EDITION, DECEMBER 2000






Inspection of

Pressure-Relieving Devices


Downstream Segment


API RECOMMENDED PRACTICE 576 SECOND EDITION, DECEMBER 2000






SPECIAL NOTES


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

API is not undertaking to meet the duties of employers, manufacturers, or suppliers to warn and properly train and equip their employees, and others exposed, concerning health and safety risks and precautions, nor undertaking their obligations under local, state, or fed- eral laws.

Information concerning safety and health risks and proper precautions with respect to par- ticular materials and conditions should be obtained from the employer, the manufacturer or supplier of that material, or the material safety data sheet.

Nothing contained in any API publication is to be construed as granting any right, by implication or otherwise, for the manufacture, sale, or use of any method, apparatus, or prod- uct covered by letters patent. Neither should anything contained in the publication be con- strued as insuring anyone against liability for infringement of letters patent.

Generally, API standards are reviewed and revised, reaffirmed, or withdrawn at least every five years. Sometimes a one-time extension of up to two years will be added to this review cycle. This publication will no longer be in effect five years after its publication date as an operative API standard or, where an extension has been granted, upon republication. Status of the publication can be ascertained from the API Standards Department [telephone (202) 682-8000]. A catalog of API publications and materials is published annually and updated quarterly by API, 1220 L Street, N.W., Washington, D.C. 20005.

This document was produced under API standardization procedures that ensure appropri- ate notification and participation in the developmental process and is designated as an API standard. Questions concerning the interpretation of the content of this standard or com- ments and questions concerning the procedures under which this standard was developed should be directed in writing to the general manager of the Standards Department, American Petroleum Institute, 1220 L Street, N.W., Washington, D.C. 20005. Requests for permission to reproduce or translate all or any part of the material published herein should also be addressed to the general manager.

API standards are published to facilitate the broad availability of proven, sound engineer- ing and operating practices. These standards are not intended to obviate the need for apply- ing sound engineering judgment regarding when and where these standards should be utilized. The formulation and publication of API standards 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 prod- ucts do in fact conform to the applicable API standard.


All rights reserved. No part of this work may be reproduced, stored in a retrieval system, or transmitted by any means, electronic, mechanical, photocopying, recording, or otherwise, without prior written permission from the publisher. Contact the Publisher,

API Publishing Services, 1220 L Street, N.W., Washington, D.C. 20005.

Copyright © 2000 American Petroleum Institute


FOREWORD


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 federal, state, or municipal regulation with which this publication may conflict.

Suggested revisions are invited and should be submitted to the manager of the Standards Department, American Petroleum Institute, 1220 L Street, N.W., Washington, D.C. 20005.


iii


CONTENTS


Page

1

SCOPE . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .

1

2

REFERENCES . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .

. 1

3

DEFINITIONS. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .

. 1

3.1 General . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .

. 1

3.2 Dimensional Characteristics of Pressure Relief Valves . . . . . . . . . . . . . . . . . . .

. 1

3.3 Operational Characteristics—System Pressures . . . . . . . . . . . . . . . . . . . . . . . . .

. 2

3.4 Operational Characteristics—Device Pressures . . . . . . . . . . . . . . . . . . . . . . . . .

. 2

4

PRESSURE-RELIEVING DEVICES . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .

. 3

    1. Pressure Relief Valve 3

    2. Safety Valve 3

    3. Relief Valve 4

    4. Safety Relief Valve 5

    5. Conventional Safety Relief Valve 5

    6. Balanced Safety Relief Valve. 5

    7. Pilot-operated Pressure Relief Valve 5

    8. Pressure and/or Vacuum Vent Valve 8

    9. Rupture Disk Device 8

  1. CAUSES OF IMPROPER PERFORMANCE 15

    1. Corrosion 15

    2. Damaged Seating Surfaces 15

    3. Failed Springs 15

    4. Improper Setting and Adjustment 17

    5. Plugging and Sticking 20

    6. Misapplication of Materials 22

    7. Improper Location, History, or Identification 23

    8. Rough Handling 23

    9. Improper Differential Between Operating and Set Pressures 24

    10. Improper Discharge Piping Test Procedures 25

  2. INSPECTION AND TESTING 25

    1. Reasons for Inspection 25

    2. Shop Inspection/overhaul 25

    3. Visual On-stream Inspection 33

    4. Inspection Frequency 34

    5. Time of Inspection 35

  3. RECORDS AND REPORTS 35

    1. Objective 35

    2. The Need to Keep Records 35

    3. Responsibilities 36

    4. Sample Record and Report System 36

Page

APPENDIX A SAMPLE RECORD AND REPORT FORMS 37

APPENDIX B PRESSURE RELIEF VALVE TESTING 45


Figures

  1. Full-Nozzle, Top-Guided Safety Valve 4

  2. Relief Valve 4

  3. Safety Relief Valve with O-Ring Seal 6

  4. Conventional Safety Relief Valve 7

  5. Balanced Bellows Safety Relief Valve 7

  6. Balanced Bellows Safety Relief Valve with Auxiliary

    Balancing Piston 8

  7. Low-Pressure Diaphragm-Type Pilot-Operated Valve 9

  8. High-Pressure Pilot-Operated Valve 10

  9. High-Pressure Pilot-Operated Valve with Optional Dual Outlets 11

  10. Weight-Loaded Pallet Vent Valve 12

  11. Spring-and Weight-Loaded Vent Valve 12

  12. Rupture Disk Device—Rupture Disk in a Typical Holder 13

  13. Conventional Domed Rupture Disk 13

  14. Scored Tension-Loaded Rupture Disk 14

  15. Reverse-Acting Scored Rupture Disk 16

  16. Reverse-Acting Rupture Disk with Knife Blades 17

  17. Graphite Rupture Disk 18

  18. Combination of Reverse-Buckling Disk Assembly and Safety Relief Valve 19

  19. Acid Corrosion in Carbon-Steel Bonnet Caused by Leaking Seating Surfaces . . 19

  20. Acid Corrosion on 18Cr-8Ni Steel Inlet Nozzle 19

  21. Chloride Corrosion on 18Cr-8Ni Steel Nozzle

    (with Machined Seating Surface) 19

  22. Sulfide Corrosion on Carbon-Steel Disk From Crude-Oil Distillation Unit 20

  23. Chloride Attack on 18Cr-8Ni Steel Disk 20

  24. Pit-Type Corrosion on 18Cr-8Ni Steel (Type 316) Bellows 20

  25. Monel Rupture Disks Corroded in Sour-Gas Service 21

  26. Body and Bonnet Coated With Epoxy for Corrosion Protection 21

  27. Seating Surface of Disk Deformed by Chattering 21

  28. Seat and Disk Damaged by Frequent Operation of Valve

    Set Too Close to Operating Pressure 21

  29. Spring Failure Due to Corrosion 22

  30. Spring Failure Due to Stress Corrosion 22

  31. Inlet Nozzle Plugged with Coke and Catalyst After Nine

    Months in Reactor Vapor Line 22

  32. Outlet Valve Plugged with Deposits From Other

    Valves in Common Discharge Header 23

  33. Moving Parts of Valve Fouled with Iron Sulfide (FeS2) 23

  34. Valve Stuck Because of Iron Sulfide (FeS2) Deposits 24

  35. Disk Frozen in Guide Because of Buildup of Products of

    Corrosion in Sour-Oil Vapor Service 24

  36. Rough Handling of Valves Should Be Avoided 24

  37. Identification Tag for Pressure- Relieving Device 26

  38. Block Valves on Safety-Relief-Valve Inlet and Outlet Sealed Open

    and Bleeders Installed to Depressure Inlet and Outlet 27

  39. Sulfur Deposits in Body of Valve on Way to Repair Shop 28

  40. Safety-Valve and Relief-Valve Leak Detector 31

B-1 Typical Safety-Valve and Relief-Valve Test Block Using Air as Test Medium. . . 46

Inspection of Pressure-Relieving Devices


  1. Scope

    This recommended practice describes the inspection and repair practices for automatic pressure-relieving devices com- monly used in the oil and petrochemical industries. As a guide to the inspection and repair of these devices in the user's plant, it is intended to ensure their proper performance. This publication covers such automatic devices as pressure relief valves, pilot-operated pressure relief valves, rupture disks, and weight-loaded pressure vacuum vents.

    The scope of this recommended practice includes the inspection and repair of automatic pressure-relieving devices commonly used in the oil and petrochemical industry.

    The recommendations in this publication are not intended to supersede requirements established by regulatory bodies. This publication does not cover weak seams or sections in tanks, explosion doors, fusible plugs, control valves, and other devices that either depend on an external source of power for operation or are manually operated. Inspections and tests made at manufacturers' plants, which are usually covered by codes or purchase specifications, are not covered by this publication.

    This publication does not cover training requirements for mechanics involved in the inspection and repair of pressure- relieving devices. Those seeking these requirements should see API 510, which gives the requirements for a quality con- trol system and specifies that the repair organization maintain and document a training program ensuring that personnel are qualified.


  2. References

    This following standards and specifications are cited in this recommended practice:

    510

    Pressure Vessel Inspection Code: Inspec-

    tion, Rating, Repair, and Alteration

    RP 520

    Sizing, Selection, and Installation of Pres- sure-Relieving Devices in Refineries, Part I, "Sizing and Selection," and Part II, "Installation"

    RP 521

    Guide for Pressure-Relieving and Depres-

    API


    suring Systems

    Std 526 Flanged Steel Pressure Relief Valves

    Std 527 Seat Tightness of Pressure Relief Valves


    Bull 2521 Use of Pressure-Vacuum Vent Valves for Atmospheric Pressure Tanks to Reduce Evaporation Loss

    ASME1

    PTC 25 Pressure Relief Devices Boiler and Pressure Vessel Code, Section I “Power Boilers” Section IV “Heating Boilers”

    Section VI “Recommended Rules for Care and Opera- tion of Heating Boilers”

    Section VII “Recommended Guidelines for Care of Power Boilers”

    Section VIII “Pressure Vessels,” Division 1

    NACE2

    Std MR0175 Sulfide Stress Cracking Resistant-Metallic Materials for Oil Field Equipment

    NB3

    NB-18 Pressure Relief Device Certifications

    NB-23 National Board Inspection Code


  3. Definitions


    1. GENERAL

      1. car seal: A self-locking seal that when placed in position and closed, locks and must be cut with wire cutters or physically broken to be removed. Local jurisdictional requirements may specify the acceptable method(s) of sealing or locking block valves.

      2. non-reclosing pressure relief device: A pres- sure relief device, which remains open after operation. A manual resetting means may be provided.

      3. pin-actuated device: A non-reclosing pressure relief device actuated by static pressure and designed to func- tion by buckling or breaking a pin which holds a piston or a plug in place. Upon buckling or breaking of the pin, the pis- ton or plug instantly moves to the full open position.


    2. DIMENSIONAL CHARACTERISTICS OF PRESSURE RELIEF VALVES

      1. effective discharge area: A nominal or computed area used with an effective discharge coefficient to calculate

Std 620 Design and Construction of Large, Welded,

Low-Pressure Storage Tanks

Std 650 Welded Steel Tanks for Oil Storage

Std 2000 Venting Atmospheric and Low-Pressure Storage Tanks (Nonrefrigerated and Refrigerated)

1

  1. ASME International, Three Park Avenue New York, New York 10016-5990, www.asme.org.

  2. NACE International, 440 South Creek Drive, Houston, Texas, 77084, www.nace.org.

  3. National Board of Boiler and Pressure Vessel Inspectors, 1055 Crupper Avenue, Columbus, Ohio 43229, www.nationalboard.com.