• BS ISO 13704:2001

    Superseded A superseded Standard is one, which is fully replaced by another Standard, which is a new edition of the same Standard.

    Petroleum and natural gas industries. Calculation of heater-tube thickness in petroleum refineries

    Available format(s):  Hardcopy, PDF

    Superseded date:  31-01-2008

    Language(s):  English

    Published date:  21-05-2004

    Publisher:  British Standards Institution

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    Table of Contents - (Show below) - (Hide below)

    Foreword
    Introduction
    1 Scope
    2 Terms and definitions
    3 General design information
       3.1 Information required
       3.2 Limitations for design procedures
    4 Design
       4.1 General
       4.2 Equation for stress
       4.3 Elastic design (lower temperatures)
       4.4 Rupture design (higher temperatures)
       4.5 Intermediate temperature range
       4.6 Minimum allowable thickness
       4.7 Minimum and average thickness
       4.8 Equivalent tube metal temperature
       4.9 Return bends and elbows
    5 Allowable stresses
       5.1 General
       5.2 Elastic allowable stress
       5.3 Rupture allowable stress
       5.4 Rupture exponent
       5.5 Yield and tensile strengths
       5.6 Larson-Miller parameter curves
       5.7 Limiting design metal temperature
       5.8 Allowable stress curves
    6 Sample calculations
       6.1 Elastic design
       6.2 Thermal-stress check (for elastic range only)
       6.3 Rupture design with constant temperature
       6.4 Rupture design with linearly changing temperature
    Annex A (informative) Estimation of remaining tube life
    Annex B (informative) Calculation of maximum radiant section
                          tube skin temperature
    Annex C (normative) Thermal-stress limitations (elastic range)
    Annex D (informative) Calculation sheets
    Annex E (normative) Stress curves (SI units)
    Annex F (normative) Stress curves (US customary units)
    Annex G (informative) Derivation of corrosion fraction and
                          temperature fraction
    Annex H (informative) Data sources
    Bibliography

    Abstract - (Show below) - (Hide below)

    Specifies the requirements and gives recommendations for the procedures and design criteria used for calculating the required wall thickness of new tubes for petroleum refinery heaters.

    General Product Information - (Show below) - (Hide below)

    Committee PSE/17
    Development Note Supersedes 99/713284 DC (01/2002)
    Document Type Standard
    Publisher British Standards Institution
    Status Superseded
    Superseded By
    Supersedes

    Standards Referencing This Book - (Show below) - (Hide below)

    ASME PV CODE 8 DIV 2 : 2017 BOILER AND PRESSURE VESSEL CODE - RULES FOR CONSTRUCTION OF PRESSURE VESSELS DIVISION 2- ALTERNATIVE RULES
    ASTM A 376/A376M : 2017 : REDLINE Standard Specification for Seamless Austenitic Steel Pipe for High-Temperature Service
    ASTM A 200 : 1994 Specification for Seamless Intermediate Alloy-Steel Still Tubes for Refinery Service (Withdrawn 1999)
    ASME B31.3:2016 PROCESS PIPING
    API 941 : 2016 STEELS FOR HYDROGEN SERVICE AT ELEVATED TEMPERATURES AND PRESSURES IN PETROLEUM REFINERIES AND PETROCHEMICAL PLANTS
    API 530 : 2015 CALCULATION OF HEATER-TUBE THICKNESS IN PETROLEUM REFINERIES
    ASTM A 312/A312M : 2017-03 SPECIFICATION FOR SEAMLESS, WELDED, AND HEAVILY COLD WORKED AUSTENITIC STAINLESS STEEL PIPES
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