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BS ISO 13704:2001

Superseded
Superseded

A superseded Standard is one, which is fully replaced by another Standard, which is a new edition of the same Standard.

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superseded

A superseded Standard is one, which is fully replaced by another Standard, which is a new edition of the same Standard.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Superseded date

01-31-2008

Language(s)

English

Published date

05-21-2004

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

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.

Committee
PSE/17
DevelopmentNote
Supersedes 99/713284 DC (01/2002)
DocumentType
Standard
Pages
148
PublisherName
British Standards Institution
Status
Superseded
SupersededBy
Supersedes

Standards Relationship
API 530 : 2015 Identical
ISO 13704:2007 Identical

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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