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API Std 521

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API Std 521 Guide for Pressure-relieving and Depressuring Systems: Petroleum petrochemical and natural gas industries-Pressure relieving and depressuring systems, Fifth Edition (Includes 2008 Addendum)

standard by American Petroleum Institute, 01/01/2007

Full Description

API 521 is applicable to pressure-relieving and vapor-depressuring systems. Although intended for use primarily in oil refineries, it is also applicable to petrochemical facilities, gas plants, liquefied natural gas (LNG) facilities and oil and gas production facilities. The information provided is designed to aid in the selection of the system that is most appropriate for the risks and circumstances involved in various installations. This standard is intended to supplement the practices set forth in API RP 520-I or ISO 4126 for establishing a basis of design.

API 521 specifies requirements and gives guidelines for examining the principal causes of overpressure; determining individual relieving rates; and selecting and designing disposal systems, including such component parts as piping, vessels, flares, and vent stacks. This Standard does not apply to direct-fired steam boilers.

This edition of API 521 is the identical national adoption of ISO 23251, Petroleum and natural gas industries-Pressure-relieving and depressuring systems

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ISO TC 67/SC 6


Pressure-relieving and Depressuring Systems


ANSI/API STANDARD 521 FIFTH EDITION, JANUARY 2007

(INCLUDES ERRATA JUNE 2007) ADDENDUM, MAY 2008


ISO 23251 (Identical), Petroleum and natural gas industries—Pressure-relieving and depressuring systems



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.


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 © 2006, 2008 American Petroleum Institute


API Foreword

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 product covered by letters patent. Neither should anything contained in the publication be construed as insuring anyone against liability for infringement of letters patent.


This document was produced under API standardization procedures that ensure appropriate notification and participation in the developmental process and is designated as an API standard. Questions concerning the interpretation of the content of this publication or comments and questions concerning the procedures under which this publication was developed should be directed in writing to the Director of Standards, 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 director.


Generally, API standards are reviewed and revised, reaffirmed, or withdrawn at least every five years. A one-time extension of up to two years may be added to this review cycle. 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 by API, 1220 L Street, N.W., Washington, D.C. 20005.

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


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Contents Page

API Foreword ii

Foreword v

Introduction vi

  1. Scope 1

  2. Normative references 1

  3. Terms and definitions 1

  4. Causes of overpressure 10

    1. General 10

    2. Overpressure protection philosophy 10

    3. Potentials for overpressure 11

    4. Recommended minimum relief system design content 17

    5. List of items required in flare-header calculation documentation 20

    6. Guidance on vacuum relief 20

  5. Determination of individual relieving rates 22

    1. Principal sources of overpressure 22

    2. Sources of overpressure 24

    3. Effects of pressure, temperature, and composition 24

    4. Effect of operator response 24

    5. Closed outlets 24

    6. Cooling or reflux failure 25

    7. Absorbent flow failure 26

    8. Accumulation of non-condensables 26

    9. Entrance of volatile material into the system 26

    10. Failure of process stream automatic controls 27

    11. Abnormal process heat input 29

    12. Internal explosion (excluding detonation) 30

    13. Chemical reaction 30

    14. Hydraulic expansion 31

    15. External pool fires 36

    16. Jet fires 51

    17. Opening manual valves 52

    18. Electric power failure 52

    19. Heat-transfer equipment failure 52

    20. Vapour depressuring 55

    21. Special considerations for individual pressure-relief devices 63

    22. Dynamic simulation 64

    23. Overfilling process or surge vessel 65

  6. Selection of disposal systems 66

    1. General 66

    2. Fluid properties that influence design 66

    3. Atmospheric discharge 67

    4. Disposal by flaring 77

    5. Disposal to a lower-pressure system 96

    6. Disposal of liquids and condensable vapours 97

    7. Disposal through common vent stack 98

  7. Disposal systems 99

    1. Definition of system design load 99

    2. System arrangement 102

    3. Design of disposal system components 104

    4. Flare gas recovery systems 141

Annex A (informative) Determination of fire relief requirements 146

Annex B (informative) Special system design considerations 150

Annex C (informative) Sample calculations for sizing a subsonic flare stack 153

Annex D (informative) Typical details and sketches 170

Annex E (informative) High integrity protection systems (HIPS) 173

Bibliography 180


Foreword


ISO (the International Organization for Standardization) is a worldwide federation of national standards bodies (ISO member bodies). The work of preparing International Standards is normally carried out through ISO technical committees. Each member body interested in a subject for which a technical committee has been established has the right to be represented on that committee. International organizations, governmental and non-governmental, in liaison with ISO, also take part in the work. ISO collaborates closely with the International Electrotechnical Commission (IEC) on all matters of electrotechnical standardization.


International Standards are drafted in accordance with the rules given in the ISO/IEC Directives, Part 2.


The main task of technical committees is to prepare International Standards. Draft International Standards adopted by the technical committees are circulated to the member bodies for voting. Publication as an International Standard requires approval by at least 75 % of the member bodies casting a vote.


Attention is drawn to the possibility that some of the elements of this document may be the subject of patent rights. ISO shall not be held responsible for identifying any or all such patent rights.


ISO 23251 was prepared by Technical Committee ISO/TC 67, Materials, equipment and offshore structures for petroleum, petrochemical and natural gas industries, Subcommittee SC 6, Processing equipment and systems.


This corrected version of ISO 23251:2006 incorporates corrections to Table 4, column 2, second row under the header, and the five rows of data in column 3.


v


Introduction


This International Standard is based on the draft 5th edition of API RP 521, with the intent that the 6th edition of API RP 521 will be identical to this International Standard.


The portions of this International Standard dealing with flares and flare systems are an adjunct to API Std 537 [10], which addresses mechanical design, operation and maintenance of flare equipment. It is important for all parties involved in the design and use of a flare system to have an effective means of communicating and preserving design information about the flare system. To this end, API has developed a set of flare data sheets, which can be found in of API Std 537, Appendix A. The use of these data sheets is both recommended and encouraged as a concise, uniform means of recording and communicating design information.


vi


API Standard 521 / ISO 23251



Petroleum, petrochemical and natural gas industries — Pressure- relieving and depressuring systems


  1. Scope


    This International Standard is applicable to pressure-relieving and vapour-depressuring systems. Although intended for use primarily in oil refineries, it is also applicable to petrochemical facilities, gas plants, liquefied natural gas (LNG) facilities and oil and gas production facilities. The information provided is designed to aid in the selection of the system that is most appropriate for the risks and circumstances involved in various installations. This International Standard is intended to supplement the practices set forth in ISO 4126 or API RP 520-I for establishing a basis of design.


    This International Standard specifies requirements and gives guidelines for examining the principal causes of overpressure; and determining individual relieving rates; and selecting and designing disposal systems, including such component parts as piping, vessels, flares, and vent stacks. This International Standard does not apply to direct-fired steam boilers.


    Piping information pertinent to pressure-relieving systems is presented in 7.3.1.


  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.


    ISO 4126 (all parts), Safety devices for protection against excessive pressure


    API RP 520-I:2000, Sizing, Selection and Installation of Pressure-Relieving Devices in Refineries — Part I: Sizing and Selection 1)


  3. Terms and definitions


For the purposes of this document, the following terms and definitions apply.


3.1

accumulation

pressure increase over the maximum allowable working pressure of the vessel allowed during discharge through the pressure-relief device


NOTE Accumulation is expressed in units of pressure or as a percentage of MAWP or design pressure. Maximum allowable accumulations are established by pressure-design codes for emergency operating and fire contingencies.



1) American Petroleum Institute, 1220 L Street, N.W., Washington, D.C., 20005-4070, USA.



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