Engineering Assessment Form* - ClockSpring|NRI · 2020. 5. 5. · B31-3 pipe calc Revised 10/16/06...

12
5 1.05 inches 0.154 inches 10 psi 100 °F 10 psi 60 °F 45 psi 350 °F 0 °F inches inches inches inches inches inches in/yr in/yr 0.33 inches inches 0.1 inches inches inches inches inches inches Repair Classification Above Ground No Repair Environment Axial Slot Length Include Top Coat No Requested Repair Length Maximum Repair Length Include Pig Markers Hydrocarbon Design Method ASME PCC-2 Cyclic Frequency Moderate Hoop Slot Length Total Affected defect Length Installation (Skin) Temperature Defect Information years Temporary [email protected] No Include Job Supervision No Component Shape Product in Pipe Defect Location Toe of weld at 3/4" sockolet Straight Pipe Planned Surface Prep** Nom. Wall Thickness Pipe Grade (SMYS) A53 Grade B Standard Environment None Internal Wall Loss Cause Max Height Differential Design Temperature (min) Phone: +1 281 590 8491 E-mail: [email protected] 621 Lockhaven Drive | Houston, TX 77073 Contact Number Contact Name Shipping Address Contact Company Name 419-698-7469 Toledo Refining Company Ed Schettler 1819 Woodville Rd. Oregon, OH 43616 Contact E-mail Project Name / Line ID Pipe Information Mechanical - acceptable Ext. Wall Loss Width Operating Temperature Mech. Damage Width Consider External Loads No Internal Wall Loss Amount Ext. Wall Loss Cause Ext. Wall Loss Length System Design Pressure Installation Pressure Operating Pressure Pipe Material Carbon Steel Piping Standard B31.3 - process piping Repair Type Location of Pipe Seam Weld Type **All products were tested to a minimum of SSPC-SP11 "Power Tool Cleaning to Bare Metal" Leak Stop Method De-pressurized Seam Weld Interaction Girth Weld Interaction Defect affecting weld Defect close to weld Inspector's Name Internal Wall Loss Width External Erosion Rate Internal Wall Loss Rate Mechanical Damage External Vibration Mech. Damage Length Date Ext. Wall Loss Depth Additional Information (optional) Internal Wall Loss Length 5/5/2020 Scott Staton *The provided information will be used to perform a design assessment - inaccurate information may lead to an incorrect design Leak Repair - Slot Intended Service Life 3/4"CA-3103 Sat Gas Suction Engineering Assessment Form* Owner / Operator Toledo Refining Company Priority Status Standard (<24 hours) Project Information Obstacles Present No Stocked Material Available Defect Scenario Single Defect Preferred Units Imperial Include Training Other Considerations Nominal Pipe Size Design Temperature (max)

Transcript of Engineering Assessment Form* - ClockSpring|NRI · 2020. 5. 5. · B31-3 pipe calc Revised 10/16/06...

  • 5

    1.05 inches

    0.154 inches

    10 psi 100 °F

    10 psi 60 °F

    45 psi 350 °F

    0 °F

    inches inches

    inches inches

    inches inches

    in/yr in/yr

    0.33 inches inches

    0.1 inches inches

    inches inches

    inches

    inches

    Repair Classification

    Above Ground

    No

    Repair Environment

    Axial Slot Length

    Include Top Coat No

    Requested Repair Length

    Maximum Repair Length

    Include Pig Markers

    Hydrocarbon

    Design Method ASME PCC-2

    Cyclic Frequency Moderate

    Hoop Slot Length

    Total Affected defect Length

    Installation (Skin) Temperature

    Defect Information

    yearsTemporary

    [email protected]

    No

    Include Job Supervision No

    Component Shape

    Product in Pipe

    Defect Location Toe of weld at 3/4" sockoletStraight Pipe

    Planned Surface Prep**

    Nom. Wall Thickness

    Pipe Grade (SMYS) A53 Grade B

    Standard Environment

    NoneInternal Wall Loss Cause

    Max Height Differential

    Design Temperature (min)

    Phone: +1 281 590 8491 E-mail: [email protected]

    621 Lockhaven Drive | Houston, TX 77073

    Contact Number

    Contact Name

    Shipping Address

    Contact Company Name

    419-698-7469

    Toledo Refining CompanyEd Schettler

    1819 Woodville Rd. Oregon, OH 43616

    Contact E-mail

    Project Name / Line ID

    Pipe Information

    Mechanical - acceptable

    Ext. Wall Loss Width

    Operating Temperature

    Mech. Damage Width

    Consider External Loads No

    Internal Wall Loss Amount

    Ext. Wall Loss Cause

    Ext. Wall Loss Length

    System Design Pressure

    Installation Pressure

    Operating Pressure

    Pipe Material Carbon Steel

    Piping Standard B31.3 - process piping

    Repair Type

    Location of Pipe

    Seam Weld Type

    **All products were tested to a minimum of SSPC-SP11 "Power Tool Cleaning to Bare Metal"

    Leak Stop Method De-pressurized

    Seam Weld Interaction

    Girth Weld Interaction Defect affecting weld

    Defect close to weld

    Inspector's Name

    Internal Wall Loss Width

    External Erosion Rate Internal Wall Loss Rate

    Mechanical Damage External Vibration

    Mech. Damage Length

    Date

    Ext. Wall Loss Depth

    Additional Information (optional)

    Internal Wall Loss Length

    5/5/2020Scott Staton

    *The provided information will be used to perform a design assessment - inaccurate information may lead to an incorrect design

    Leak Repair - Slot

    Intended Service Life

    3/4"CA-3103 Sat Gas Suction

    Engineering Assessment Form*

    Owner / Operator Toledo Refining CompanyPriority Status Standard (

  • EXISTING PIPING SYSTEM ANALYSIS1ASME B31.3 INTERNAL PRESSURE PIPE CALCULATIONS2004 Edition

    PROJECT INPUTProject number By Date

    Customer or Client Case or Page Number

    Project Description

    Notes or design basis description

    DESIGN DATA INPUT

    Line number (size, class & sequential number)ASTM pipe material

    Design temperature (degrees F)P = Internal design gage pressure (PSIG)D = Outside diameter of pipe (inches)E = Quality factor - from Table A-1A or A-1BY = Coefficient from Table 304.1.1S = Allowable stress value at design temperature (KSI) - from Table A-1

    S T = Allowable stress value at test temperature (KSI) - from Table A-1

    Future corrosion allowance (inches)Future erosion allowance (inches)Thread or groove depth (inches) - from ASME B1.20.1 (dimension h )Other allowance (inches) Describe:

    T = Field-measured (UT or RT) existing, available wall thickness (inches)

    STRAIGHT PIPE REQUIRED THICKNESSParagraph 304.1 (pg. 19)

    t m = or t m = Minimum required thickness1 (inches)

    Where:

    c = Sum of mechanical allowances

    Differential between available wall and t m - MUST be a positive number(to confirm adequate thickness is available)

    HYDROSTATIC LEAK TESTParagraph 345.4.2 (pg. 78)

    NOTE:1)

    16.0

    0.0000.000

    0.000

    =

    0.001

    68

    =

    0.136

    80133496

    3/4" Vent on 12"CA-3103

    SA-53

    5/4/2020E. Schettler

    3/4"CA-3103

    Toledo Refinery

    P T

    2(SE + PY) or

    = 1.5 P S TS

    t

    or

    Minimum thickness calculations do not take into account system structural or thermal stresses. API Recommended Practice 579 includes other factors (brittle fracture, pitting, blisters/laminations, weld misalignment, distortions, cracks, creep) to be considered when determining fitness-for-service.

    c =0.0000.000

    Minimum test gage pressure (PSIG)

    0.001t + c

    Pressure design thickness as calculated per para. 304.1.2 (3a)

    P T

    0.400

    350.000

    t

    0.137

    = PD

    45.0001.0501.000

    16.0

    B31-3 pipe calcRevised 10/16/06 by D.Stieb to reference 2004 edition of B31.3 and to include "Y" coefficient in thickness calculation.

  • Crushing Calculation

    INFORMATION

    PlantLine NumberClamp NumberComponent Design

    σsh ALLOWABLE SHELL STRESS (PSI) ~REF.1 E MODULUS OF ELASTICITY (PSI)Do PIPE OUTSIDE DIAMETER (IN) Ri INSIDE RADIUS (IN)tn NORMAL PIPE WALL THICKNESS (IN) Ro OUTSIDE RADIUS (IN)Ca CORROSION ALLOWANCE (IN)Pd DESIGN PRESSURE (PSIG)Td DESIGN TEMPERATURE (°F)

    A. CONSTANTS E= 30000000

    Pd: = 45 Td: = 350 σsh: = 16000

    B. VARIABLES

    Do: = 1.05 tn: = 0.154 Ca: = 0.084

    PIPE SECTION ANALYSIS

    A. MINIMUM PIPE WALL THICKNESS WITH CORROSION ALLOWANCE (tmin) - (IN)

    tmin: = tn-Ca tmin = 0.07

    Do - 2 x tmin Ri Ri2 tmin tmin

    Ri = 0.455Ri 0=PIPE IS THICK WALLED

    Do tmin 1=PIPE IS THIN WALLED22

    tminthk= 0.048

    2 2Do2

    2

    MAXIMUM ALLOWABLE EXTERNAL PRESSURE A THICK WALLED PIPE

    MWe=

    MWe=

    2 x Ri

    σsh

    MAXIMUM ALLOWABLE EXTERNAL PRESSURE A THICK WALLED PIPE CAN WITH STAND (Mwe) -(PSI) ~REF.2

    PSI

    412"CA-3103

    ≤ 10 = 0 > 10 =1

    = 6.500

    2650.888

    tminthk: =

    -Ri

    Ri =

  • Do Do2 22

    Ro= 0.525 tmax= 0.048

    Ro 0.525σsh 16000 tminE 30000000 Ro 2

    4 x σsh RoE tmin

    MAXIMUM ALLOWABLE EXTERNAL PRESSURE A THIN WALLED PIPE

    PSIMWe= 1904.762

    1+ x

    MWe=

    MAXIMUM ALLOWABLE EXTERNAL PRESSURE A THIN WALLED PIPE CAN WITH STAND (Mwe) -(PSI) ~REF.2

    x σsh

    Ro= tmax=

  • Expected Remaining Pipe Life

    Pipe Size  0.75 inchOriginal Pipe Wall Thickness  0.154 inchT‐min of Pipe Per B31.3 Calc's 0.07 inchMin Inspection Field Measurement 0.137 inchApprox. Date Pipe Was Installed  1989Year for First Hole Through  2020

    Years of service before First Hole Through  31 years 

    Wall Loss based off of Inspection Data 0.017 inch 

    Annual Corrosion Rate  0.0005 inch's Per Year 

    Reaming Pipe Thickness Before T‐min 0.067 inch 

    Years of Line Service Approx. Before T‐min 122.2 years @ current corrosion rate

    Additional Note's:

    From API‐574

    Note's

  • PIPING SPECIFICATIONS

    CLASS CAA

    RS-ALL-ES STD-0202

    R&S ENGINEERING STANDARDS

    Control Tier: 2-Refining & Supply

    Document Authorizer: VP Refining Excellence

    Issuing Dept: Engineering Services (ES)

    Document Reviewer: Manager, Engineering Specialists

    Revision Date: May 1, 2010 (Revised)

    Document Author: Chairperson of Engineering Standards Committee

    Next Review Date: May 1, 2015

    Document Administrator: Standards Document Control Coordinator

    REVISION LOG

    SERVICE: GENERAL PROCESS, NON-CORROSIVE

    ASME RATING: CLASS 150 RF, ASME B16.5 MAT. GROUP 1.1

    MAX PRESS/MAX TEMP: 285# / AMBIENT, 110# / 700°F (A)

    GENERAL MATERIAL: CARBON STEEL, VALVE TRIM: API #1

    CORROSION ALLOWANCE: 0.05 IN.

    PWHT REQUIRED: NO

    PIPE

    3/4" - 1 1/2" SCH. 160, SEAMLESS STEEL, ASTM A106 GR. B

    2" SCH. 80, SEAMLESS STEEL, ASTM A106 GR. B

    3" - 24" STD. WALL, SEAMLESS STEEL, ASTM A106 GR. B

    VALVES

    GATE 3/4" - 2" TAG NO.: V31CH-1 CLASS 800, CS, OS&Y, BB, THREADED

    3/4" - 2" TAG NO.: V31CH-2 CLASS 800, CS, OS&Y, BB, SOCKET WELD

    3/4" - 2" TAG NO.: V31CH-13 CLASS 800, CS, OS&Y, BB, SOCKET WELD/FEMALE THD

    3" - 24" TAG NO.: V41C-4 CLASS 150, CS, OS&Y, BB, RAISED FACE

    GLOBE 3/4" - 2" TAG NO.: V131CH-1 CLASS 800, CS, OS&Y, BB, THREADED

    3/4" - 2" TAG NO.: V131CH-2 CLASS 800, CS, OS&Y, BB, SOCKET WELD

    3" - 12" TAG NO.: V141C-4 CLASS 150, ANSI, CS, OS&Y, BB, RAISED FACE

    BALL 3/4" - 2" TAG NO.: VBA602T-1 CLASS 600, 400°F MAX, CS BODY, TEFLON SEAL, LEVER OPER, THREADED

    3" - 8" TAG NO.: VBA151T-4 CLASS 150, 400°F MAX, CS BODY, TEFLON SEAL, LEVER OPER, RAISED FACE

    10" - 16" TAG NO.: VBA151T-4 CLASS 150, 400°F MAX, CS BODY, TEFLON SEAL, GEAR OPER, RAISED FACE

    http://pcsweb13/SES/es/esstd0202scaa.htm#RevisionLog#RevisionLog

  • CHECK (C) 3/4" - 2" TAG NO.: V231CH-1 CLASS 800, CS, BALL CHECK, BB, THREADED

    3/4" - 2" TAG NO.: V231CH-2 CLASS 800, CS, BALL CHECK, BB, SOCKET WELD

    3" - 18" TAG NO.: V241C-4 CLASS 150, ANSI, CS, SWING CHECK, BB, RAISED FACE

    3" - 24" TAG NO.: VWC151 CLASS 150, CS, DUAL PLATE, INCONEL X SPRING, FLANGELESS, RAISED FACE

    PLUG 3/4" - 2" TAG NO.: V331-1 CLASS 300, 350°F MAX, CS BODY, WRENCH OPER, THREADED

    2-1/2" - 6" TAG NO.: V341-4 CLASS 150, 350°F MAX, CS BODY, WRENCH OPER, RAISED FACE

    2-1/2" - 6" TAG NO.: V344-4 CLASS 150, 500°F MAX, CS BODY, WRENCH OPER, RAISED FACE

    8" - 12" TAG NO.: V342-4 CLASS 150, 350°F MAX, CS BODY, GEAR OPER, RAISED FACE

    8" - 12" TAG NO.: V345-4 CLASS 150, 500°F MAX, CS BODY, GEAR OPER, RAISED FACE

    14" - 24" TAG NO.: V343-4 CLASS 150, 350°F MAX, CS BODY, GEAR OPER, RAISED FACE

    GASKETS

    CLASS 150, SPIRAL WOUND, STYLE LSI, TYPE 304, GRAFOIL FILLER, ASME B16.20

    FLANGES

    ORIFICE 3/4" - 24" CLASS 300, FS, WELD NECK TYPE, 1/2" NPS TAPS, RAISED FACE," ASTM A105

    PIPING 3/4" - 2" CLASS 150, FS, SOCKET WELD TYPE, RAISED FACE, ASTM A105

    3" - 24" CLASS 150, FS, WELD NECK TYPE, RAISED FACE, ASTM A105

    FITTINGS

    BUTT WELD 3" - 24" STD. WALL, SEAMLESS, ASTM A234 GR WPB

    SOCKET WELD 3/4" - 2" CLASS 3000 FS, ASTM A105

    THREADED 3/4" - 2" CLASS 3000 FS, ASTM A105

    THERMOWELL 1" CLASS 3000 FS, THREADED INTEGRALLY REINFORCED BRANCH CONNECTION FITTING, ASTM A105

    1" CLASS 6000 FS, THREADED FULL COUPLING, ASTM A105

    BOLTING

    NUTS, HEX ASTM A194 GR 2H

    STUDS THREADED FULL LENGTH, ASTM A193 GR B7

    NOTES:

    A: SEE TEMPERATURE LIMITATIONS ON BALL AND PLUG VALVES.

    B: FOR VACUUM SERVICE, GASKETS SHALL BE CORRUGATED, DOUBLE-JACKETED, GRAFOIL FILLED TO ASME B16.20 SPECIFICATIONS.

    C: DUAL PLATE CHECK VALVES SHALL BE USED ON NEW PROJECTS UNLESS OTHERWISE SPECIFIED BY THE OWNER’S PROJECT ENGINEER.

    D: FOR GENERAL NOTES SEE 0202 PREAMBLE, PART J.

    E: SCH 160 NOTE: SCHEDULE 80 CARBON STEEL PIPE MAY BE USED FOR 1" - 1 1/2" NPS WHEN APPROPRIATE

  • SUPPORTS ARE DESIGNED FOR AND DOCUMENTED BY QUALIFIED PERSONNEL TAKING INTO ACCOUNT ABNORMAL AND UNINTENTIONAL MECHANICAL LOADINGS. 1" NPS CARBON STEEL SCHEDULE 160 PIPE MAY BE USED TO ACCOUNT FOR THE REDUCED CROSS SECTION OF 3/4" NPS SCHEDULE 160 PIPING WHEN PRESSURE DROP DICTATES.

    REVISION LOG

    Revision Date Document Authorizer Document Reviewer Document Author

    Document

    Administrator Revision Details

    April 4, 2005 Beverly Valerio Added OEMS formatting

    December 8, 2006 V. Srivastava B. Chmielewski Beverly Valerio Reaffirmed

    May 1, 2010 K. Robles B. Brodwater / T. Dougher M. Fleet Beverly Valerio Revision

  • Z99EXSOval

    Z99EXSCalloutLeak Location

  • Z99EXSPolygonal Line

    Z99EXSLine

    Z99EXSPolygonal Line

    Z99EXSOval

    Z99EXSCalloutLocation of Leak

  • Z99EXSCalloutLeak Location

    2020-05-04 44-002A CML-5B31-3 pipe calcC-13190_S3103_3Class 0200 Piping STD-0202 Class CAACrushing CalculationExisting Pipe Life CalculationP1050498