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API Std 660

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API Std 660 Shell-and-tube Heat Exchangers, Ninth Edition, Includes Addendum 1 (2020)

standard by American Petroleum Institute, 03/02/2015

Full Description

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

This standard specifies requirements and gives recommendations for the mechanical design, material selection, fabrication, inspection, testing, and preparation for shipment of shell-and-tube heat exchangers for the petroleum, petrochemical, and natural gas industries.

This standard is applicable to the following types of shell-and-tube heat exchangers: heaters, condensers, coolers, and reboilers.This standard is not applicable to vacuum-operated steam surface condensers and feed-water heaters.

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Shell-and-Tube Heat Exchangers


API STANDARD 660

NINTH EDITION, MARCH 2015 ADDENDUM 1, AUGUST 2020



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.


All rights reserved. No part of this work may be reproduced, translated, 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, 200 Massachusetts Avenue, NW, Suite 1100, Washington, DC 20001.


Copyright © 2015 American Petroleum Institute


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.


Shall: As used in a standard, “shall” denotes a minimum requirement in order to conform to the specification.


Should: As used in a standard, “should” denotes a recommendation or that which is advised but not required in order to conform to the specification.


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, 200 Massachusetts Avenue, NW, Suite 1100, Washington, DC 20001. 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, 200 Massachusetts Avenue, NW, Suite 1100, Washington, DC 20001.


Suggested revisions are invited and should be submitted to the Standards Department, API, 200 Massachusetts Avenue, NW, Suite 1100, Washington, DC 20001, standards@api.org.


iii


Contents


Page

  1. Scope 1

  2. Normative References 1

  3. Terms and Definitions 1

  4. General 3

  5. Proposal Information Required 4

  6. Drawings and Other Required Data 5

    1. Outline Drawings and Other Supporting Data 5

    2. Information Required After Outline Drawings Are Reviewed 6

    3. Reports and Records 7

  7. Design 8

    1. Design Temperature 8

    2. Cladding for Corrosion Allowance 8

    3. Shell Supports 9

    4. Stationary and Floating Heads 9

    5. Tube Bundle 10

    6. Nozzles and Other Connections 15

    7. Flanged External Girth Joints 16

    8. Girth Flange Joint Supplementary Design Requirements 20

    9. Expansion Joints 22

    10. Gaskets 22

    11. Handling Devices 24

    12. Requirements for Hydrogen Service 24

  8. Materials 24

    1. General 24

    2. Requirements for Carbon Steel in Sour or Wet Hydrogen Sulfide Service 25

    3. Gaskets 25

    4. Tubes 25

  9. Fabrication 25

    1. Shells 25

    2. Pass-partition Plates 26

    3. Connection Junctions 26

    4. Tubes 26

    5. Welding 26

    6. Heat Treatment 27

    7. Dimensional Tolerances 28

    8. Gasket Contact Surfaces Other Than Nozzle Flange Facings 28

    9. Tube Holes 30

    10. Tube-to-Tubesheet Joints 30

    11. Assembly 31

      v

      Contents

      Page

  10. Inspection and Testing 31

    1. Quality Control 31

    2. Pressure Testing 34

    3. Nameplates and Stampings 34

  11. Preparation for Shipment 35

    1. Protection 35

    2. Identification 36

  12. Supplemental Requirements 36

    1. General 36

    2. Design 36

    3. Examination 36

  13. Supplemental Requirements for Services Subject to High Temperature Hydrogen Service (HTHS) . . . 37 13.1 General 37

    1. Design Temperature 37

    2. Materials 38

    3. Connections for Temperature Indication 38

    4. Fabrication 38

    5. Inspection and Testing 38

Annex A (informative) Recommended Practices 40

Annex B (informative) Shell-and-Tube Heat Exchanger Checklist 51

Annex C (informative) Shell-and-Tube Heat Exchanger Datasheets 54

Bibliography 67


Figures

  1. Minimum Thickness of Tubes 10

  2. Clearance Between Tube Holes and Transverse Baffle Edge with Longitudinal Baffle 12

  3. Typical Cross-sections of Tube Bundle Showing Locations of Bypass Sealing Devices 14

  4. Directions of Moments and Forces on Nozzles 16

Tables

  1. Typical Designs for Floating-head Covers 11

  2. Nozzle Allowable Forces and Moments at the Nozzle Neck to Shell/Channel Interface 17

  3. Assembly Gasket Stress 21

  4. Gasket Contact Surface Finishes 29

  5. Flatness Tolerance on Peripheral Gasket Contact Surfaces 29

  6. Maximum Allowable Tube Wall Thickness Reduction for Roller-expanded Tube-to-Tubesheet Joints . 30 7 Hardness Limits 32

B.1 Checklist for Shell-and-Tube Heat Exchangers 51


vi


Introduction


It is necessary that users of this standard be aware that further or differing requirements can be needed for individual applications. This standard is not intended to inhibit a vendor from offering, or the purchaser from accepting, alternative equipment or engineering solutions for the individual application. This can be particularly applicable where there is innovative or developing technology. Where an alternative is offered, the vendor should identify any variations from this standard and provide details.


This standard requires the purchaser to specify certain details and features.


A bullet () at the beginning of a section indicates a requirement for the purchaser to make a decision or provide information (for information, a checklist is provided in Annex B).


In this standard, where practical, U.S. Customary (USC) or other units are included in parentheses for information.


vii


Shell-and-Tube Heat Exchangers


  1. Scope


    This standard specifies requirements and gives recommendations for the mechanical design, material selection, fabrication, inspection, testing, and preparation for shipment of shell-and-tube heat exchangers for the petroleum, petrochemical, and natural gas industries.


    This standard is applicable to the following types of shell-and-tube heat exchangers: heaters, condensers, coolers, and reboilers.


    This standard is not applicable to vacuum-operated steam surface condensers and feed-water heaters.


  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 RP 941, Steels for Hydrogen Service at Elevated Temperatures and Pressures in Petroleum Refineries and Petrochemical Plants

    ASME B16.5 1, Pipe Flanges and Flanged Fittings: NPS 1/2 through NPS 24 Metric/Inch Standard

    ASME PCC-1-2013, Guidelines for Pressure Boundary Bolted Flange Joint Assembly

    EJMA 2, Standards of the Expansion Joint Manufacturers Association

    NACE MR0103 3, Materials Resistant to Sulfide Stress Cracking in Corrosive Petroleum Refining Environments

    NACE MR0175, Petroleum and natural gas industries—Materials for use in H2S containing environments in oil and gas production—Parts 1, 2 and 3


    NACE SP0472, Methods and Controls to Prevent In-Service Environmental Cracking of Carbon Steel Weldments in Corrosive Petroleum Refining Environments

    TEMA 4, Ninth Edition, Standards of the Tubular Exchanger Manufacturers Association


  3. Terms and Definitions


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


3.1

annular distributor

An additional chamber incorporated into a shell side nozzle to evenly distribute shell side fluids entering or exiting the tube bundle.


  1. ASME International, 2 Park Avenue, New York, New York 10016-5990, www.asme.org.

  2. Expansion Joint Manufacturers Association, 25 North Broadway, Tarrytown, New York 10591, www.ejma.org.

  3. NACE International (formerly the National Association of Corrosion Engineers), 1440 South Creek Drive, Houston, Texas 77084-4906, www.nace.org.

  4. Tubular Exchanger Manufacturers Association, 25 North Broadway, Tarrytown, New York 10591, www.tema.org.


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