UNI EN ISO 13704 : 2009
Superseded
A superseded Standard is one, which is fully replaced by another Standard, which is a new edition of the same Standard.
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PETROLEUM, PETROCHEMICAL AND NATURAL GAS INDUSTRIES - CALCULATION OF HEATER-TUBE THICKNESS IN PETROLEUM REFINERIES
16-03-2023
26-03-2009
Foreword
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 thicknesses
4.8 Equivalent tube metal temperature
4.9 Component fittings
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 (USC units)
Annex G (normative) - Derivation of corrosion fraction
and temperature fraction
Annex H (informative) - Data sources
Bibliography
Describes the requirements and gives recommendations for the procedures and design criteria used for calculating the required wall thickness of new tubes and associated component fittings for petroleum-refinery heaters.
Committee |
CT 700
|
DocumentType |
Standard
|
PublisherName |
Ente Nazionale Italiano di Unificazione (UNI)
|
Status |
Superseded
|
SupersededBy |
Standards | Relationship |
ISO 13704:2007 | Identical |
UNI/TS 11325-4 : 2013 | PRESSURE EQUIPMENT - PUTTING INTO SERVICE AND USE OF PRESSURE EQUIPMENT AND ASSEMBLIES - PART 4: OPERATIONAL METHODS FOR THE INTEGRITY ASSESSMENT OF PRESSURE EQUIPMENT WORKING UNDER CREEP CONDITIONS RELATED TO THE ASSESSMENT PROCEDURE OF THE UNI/TS 11325-2 |
UNI/TS 11325-2 : 2013 | PRESSURE EQUIPMENT - PUTTING INTO SERVICE AND USE OF PRESSURE EQUIPMENT AND ASSEMBLIES - PART 2: ASSESSMENT PROCEDURE OF FITNESS FOR SERVICE OF PRESSURE EQUIPMENT WORKING UNDER CREEP CONDITIONS |
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 |
ASME PV CODE 8 DIV 1 : 2017 | BOILER AND PRESSURE VESSEL CODE - RULES FOR CONSTRUCTION OF PRESSURE VESSELS DIVISION 1 |
ASTM A 200 : 1994 | Specification for Seamless Intermediate Alloy-Steel Still Tubes for Refinery Service (Withdrawn 1999) |
ASME B31.3:2016 | PROCESS PIPING |
ISO 13705:2012 | Petroleum, petrochemical and natural gas industries — Fired heaters for general refinery service |
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 |
ASME B16.9 : 2012 | FACTORY-MADE WROUGHT BUTTWELDING FITTINGS |
ASTM A 312/A312M : 2017-03 | SPECIFICATION FOR SEAMLESS, WELDED, AND HEAVILY COLD WORKED AUSTENITIC STAINLESS STEEL PIPES |
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