• 04/19991491 DC : DRAFT DEC 2004

    Superseded A superseded Standard is one, which is fully replaced by another Standard, which is a new edition of the same Standard.

    BS ISO 10400 - PETROLEUM AND NATURAL GAS INDUSTRIES - FORMULAE AND CALCULATION FOR CASING, TUBING, DRILL PIPE AND LINE PIPE PROPERTIES

    Available format(s): 

    Superseded date:  31-01-2008

    Language(s): 

    Published date:  23-11-2012

    Publisher:  British Standards Institution

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

    Foreword
    Introduction
    1 Scope
    2 Conformance
    3 Normative references
    4 Terms and definitions
    5 Symbols and abbreviated terms
    6 Triaxial Yield of Pipe Body
       6.1 Introduction
       6.2 Assumptions and Limitations
       6.3 Data Requirements
       6.4 Design Formula for Triaxial Yield of Pipe Body
       6.5 Example Calculations
    7 Ductile Rupture of the Pipe Body
       7.1 Introduction
       7.2 Assumptions and Limitations
       7.3 Data Requirements
       7.4 Design Formula for Ductile Rupture
       7.5 Adjustment for the Effect of Axial Tension and
             External Pressure
       7.6 Example Calculations
    8 External Pressure Resistance
       8.1 Introduction
       8.2 Assumptions and Limitations
       8.3 Data Requirements
       8.4 Design Formula for Collapse of Pipe Body
       8.5 Formulas for Empirical Constants
       8.6 Example Calculations
    9 Joint Strength
       9.1 Introduction
       9.2 Design Formulas for API Casing Connections
             Tensile Joint Strength
    10 Pressure Performance for Connections
       10.1 Design Formulas for Internal Yield Pressure
             of Couplings
       10.2 Design Formulas for Internal Pressure Leak
             Resistance at E[1] or E[7] Plane
    11 Calculated Masses
       11.1 Nominal Masses
       11.2 Calculated Plain-End Mass
       11.3 Calculated Threaded and Coupled Mass
       11.4 Calculated Upset and Threaded Mass for Integral
             Joint Tubing and Extreme-Line Casing
       11.5 Calculated Upset Mass
       11.6 Mass Gain Due to End Finishing
       11.7 Calculated Coupling Mass
       11.8 Calculated Mass Removed during Threading
       11.9 Calculated Mass of External Upsets
       11.10 Calculated Mass of Internal Upsets
       11.11 Calculated Mass of External-Internal Upsets
       11.12 Calculated Mass of External-Line Upsets
    12 Elongation
       12.1 Background
    13 Flattening Tests
       13.2 Flattening Tests for Line Pipe
    14 Hydrostatic Test Pressures
       14.1 Hydrostatic Test Pressures for plain-End Pipe,
             Extreme-Line Casing and Integral Joint Tubing
       14.2 Hydrostatic Test Pressure for Threaded and
             Coupled Pipe
    15 Make-up Torque for Round Thread Casing and Tubing
       15.1 Background
    16 Guided Bend Tests for Submerged Arc Welded Line Pipe
       16.1 Background
    17 Determination of Minimum Impact Specimen Size for
       API Couplings and Pipe
       17.1 Critical Thickness
       17.2 Calculated Coupling Blank Thickness
       17.3 Calculated Wall Thickness for Transverse
             Specimens
       17.4 Calculated Wall Thickness for Longitudinal
             Specimens
       17.5 Minimum Specimen Size for API Couplings
       17.6 Impact Specimen Size for Pipe
       17.7 Larger Size Specimens
       17.8 Reference Information
    Annex A (informative) Discussion of Formulas for
            Triaxial Yield of Pipe Body
            A.1 Triaxial Yield of Pipe Body
            A.2 Initial Yield of Pipe Body, Lame Formulation
                for Pipe when External Pressure, Bending and
                Torsion are Zero
            A.3 Initial Yield of Pipe Body, Historical API
                Formulation
    Annex B (informative) Discussion of Formulas for Ductile
            Rupture
            B.1 Introduction
            B.2 Ductile Rupture of Pipe Body
            B.3 Selection of a Ductile Rupture Model
            B.4 Pipe Rupture Data Base Used to Validate the
                Rupture Models
            B.5 Comparison Between the Different Rupture
                Models and Pipe Rupture Data Under Capped-End
                Conditions
            B.6 Comparison Between the Recommended Rupture
                Model and Pipe Rupture Data Under Capped-End
                Conditions
            B.7 The Role of Imperfections in the Ductile
                Rupture Formula
            B.8 Template for Probabillistic Calculation of
                Ductile Rupture Strength
    Annex C (normative) Rupture Test Procedure
            C.1 Specimen Ends
            C.2 Specimen Length
            C.3 Application of Pressure
    Annex D (informative) Discussion of Formulas For Fracture
            D.1 Material Induced Fracture of the Pipe Body
            D.2 Fracture due to Environmental Crack Initiation
    Annex E (informative) Discussion of Historical, API Collapse
            Formulas
            E.1 Introduction
            E.2 Collapse Pressure Formulas
            E.3 Derivation of Collapse Pressure
    Annex F (informative) Proposed Formulas for Collapse
            F.1 Draft Collapse Section of Main Text
    Annex G (informative) Discussion of Proposed Formulas for
            Collapse
            G.1 Collapse Failure of the Pipe Body
            G.2 KT Collapse Formula
            G.3 KT Collapse Formula, External pressure only
            G.4 Limitations
            G.5 Using the KT Collapse Formula as Design Formula
    Annex H (informative) Development of Proposed Formulas for
            Collapse of Q&T Pipe
            H.1 Introduction
            H.2 Selection of Ultimate Limit State Formula
            H.3 Ultimate Limit State Formula
            H.4 Input Variable PDF Types and Parameters
            H.5 Target Reliability Level
            H.6 Design Formula
            H.7 Risk-Calibrated Design Strength
    Annex I (informative) Development of Proposed Formulas
            for Collapse of non-Q&T Pipe
            I.1 Introduction
            I.2 Ultimate Limit State Formula
            I.3 Design Formulas
            I.4 Results
    Annex J (normative) Calculation Procedure for Case-Specific
            Q&T Collapse Strengths
            J.1 Introduction
            J.2 Production Quality Statistics
            J.3 Probabillistic Analysis
            J.4 Substantiation of case-Specific Strengths
    Annex K (normative) Collapse Test Procedure
            K.1 Test Specimen
            K.2 Test Apparatus
            K.3 Measurements Prior to Collapse Testing
            K.4 Test Procedure
            K.5 Data Reporting
    Annex L (informative) Discussion of Formulas for Joint
            Strength
            L.1 Introduction
            L.2 Design Formulas for API Casing Connections
                Tensile Joint Strength
    Annex M (informative) Table of Calculated Performance
            Properties
    Bibliography
    Annex N
    N.1 Burst
    N.2 Collapse

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

    Comment Closes On
    Committee PSE/17/-/5
    Document Type Draft
    Publisher British Standards Institution
    Status Superseded
    Superseded By

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

    BS 7910:1999 Guide on methods for assessing the acceptability of flaws in metallic structures
    ISO 13679:2002 Petroleum and natural gas industries Procedures for testing casing and tubing connections
    API 5D : 2001 SPECIFICATION FOR DRILL PIPE
    NACE TM 01 77 : 2016 LABORATORY TESTING OF METALS FOR RESISTANCE TO SULFIDE STRESS CRACKING AND STRESS CORROSION CRACKING IN H[2]S ENVIRONMENTS
    ISO 3183:2012 Petroleum and natural gas industries Steel pipe for pipeline transportation systems
    API 5L : 2012 LINE PIPE
    ISO 10422:1993 Petroleum and natural gas industries — Threading, gauging, and thread inspection of casing, tubing and line pipe threads — Specification
    API 579-1 : 2016 FITNESS-FOR-SERVICE
    ISO 11960:2014 Petroleum and natural gas industries Steel pipes for use as casing or tubing for wells
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