sample13 spreadsheet

Download Sample13 Spreadsheet

Post on 06-Apr-2018

214 views

Category:

Documents

0 download

Embed Size (px)

TRANSCRIPT

  • 8/2/2019 Sample13 Spreadsheet

    1/100

  • 8/2/2019 Sample13 Spreadsheet

    2/100

  • 8/2/2019 Sample13 Spreadsheet

    3/100

    Pressure Vessel Engineering, Ltd.120 Randall Dr. Waterloo, Ontario N2V 1C6

    Date Printed: 11/12/2009

  • 8/2/2019 Sample13 Spreadsheet

    4/100

    Pressure Vessel Design Summary

    Customer

    Vessel

    Job & Rev

    Calculations by

    Reviewed by

    UG-22 Loadings Considered

    Yes (a) Internal pressure

    No (a) External pressure

    No (b) Vessel weight full, empty and at hydro test

    No (c) Weight of attached equipment and piping

    No (d)(1) Attachment of internals

    No (d)(2) Attachment of vessel supports

    No (d) Cyclic or dynamic reactions

    Yes (f) Wind

    No (f) Snow

    Yes (f) SeismicNo (g) Fluid impact shock reactions

    No (h) Temperature gradients

    No (h) Differential thermal expansion

    No (i) Abnormal pressures like deflagration

    NO (j) Hydrotest Loads

    Sample 13

    Sample 13

    Brian Munn

    Laurence Brundrett P. Eng.

  • 8/2/2019 Sample13 Spreadsheet

    5/100

    Pressure Vessel Engineering, Ltd.Shell 1

    Customer: Pressure Vessel Engineering LtdJob No: PVE-3602 Sample 13 Vessel Number: Sample 13

    Number: 1 Mark Number: S1

    Date Printed: 11/12/2009

    Cylindrical Shell Design Information

    Design Pressure: 250.00 PSI Design Temperature: 550 F

    Static Head: 34.00 PSI Long. Joint Efficiency: 85 %Shell Material: SA-516 Gr. 70 Factor B Chart: CS-2

    Material Condition: Normalized Material Stress (hot): 19700 PSIShell Length: 98.0000 in. Material Stress (cold): 20000 PSI

    Compressive Stress: 11431 PSICorrosion Allowance: 0.1250 in. Actual Circumferential Stress: 16286 PSI

    External Corrosion Allowance: 0.0000 in. Actual Longitudinal Stress: 7976 PSI

    Outside Diameter (new): 86.0000 in.Outside Diameter (corroded): 86.0000 in. Specific Gravity: 1.00

    Shell Surface Area: 183.87 Sq. Ft. Weight of Fluid: 19643.09 lb.Shell Estimated Volume: 2351.32 Gal. Total Flooded Shell Weight: 26970.54 lb.

    Circ. Joint Efficiency: 85 % Shell Weight: 7327.45 lb.

    Minimum Design Metal Temperature Data

    Min. Temperature Curve: D Pressure at MDMT: 250.00 PSIUCS-66(b) reduction: No Minimum Design Metal Temperature: -20 FUCS-68(c) reduction: No Computed Minimum Temperature: -30 F

    External Pressure Data

    Design Pressure (Pa): 15.00 PSI Design Temperature: 550 FDimension L: 294.0000 in.

    Ext. Minimum t: 0.5830 in. Ext. Nominal t: 1.0000 in.Minimum L/Do: 3.4186 Nominal L/Do: 3.4186Minimum Do/t: 187.7730 Nominal Do/t: 98.2857

    Minimum Factor A:0.0001627 Nominal Factor A:0.0004162Minimum Factor B: 2112 PSI Nominal Factor B: 5414 PSI

    Design Thickness Calculations

    Longitudinal Stress Calculations per Paragraph UG-27(c)(2)

    t =PR

    2SE + 0.4P=

    284.00 * 42.1250

    2 * 19700 * 0.85 + 0.4 * 284.00= 0.3560 + 0.1250 (corrosion) + 0.0000 (ext.corrosion) = minimum of 0.4810

    Circumferential Stress Calculations per Appendix 1-1(a)(1)

    t =PRo

    SE + 0.4P=

    284.00 * 43.0000

    19700 * 0.85 + 0.4 * 284.00= 0.7244 + 0.1250 (corrosion) + 0.0000 (ext.corrosion) = minimum of 0.8494

    Maximum External Pressure Calculation per Paragraph UG-28

    Pa (using nominalt) =4B

    3(Do / t)=

    4 * 5414

    3 * ( 86.0000 / 0.8750 )= maximum external pressure of 73.45 P

    Extreme Fiber Elongation Calculation per Paragraph UCS-79

    Elongation =50t

    Rf=

    50 * 1.0000

    42.5000= elongation of 1.18

    External loads do not control design.

    Advanced Pressure Vessel version: 10.1.5 Computer Engineering, Inc. Section VIII, Division 1, 2007 Edition, 2008 AddenPage 1 of 95

  • 8/2/2019 Sample13 Spreadsheet

    6/100

    Pressure Vessel Engineering, Ltd.Shell 1

    Job No: PVE-3602 Sample 13 Vessel Number: Sample 13Number: 1 Mark Number: S1

    Date Printed: 11/12/2009

    Nominal Shell Thickness Selected = 1.0000 in.

    Advanced Pressure Vessel version: 10.1.5 Computer Engineering, Inc. Section VIII, Division 1, 2007 Edition, 2008 AddenPage 2 of 95

  • 8/2/2019 Sample13 Spreadsheet

    7/100

    Pressure Vessel Engineering, Ltd.Shell 2

    Customer: Pressure Vessel Engineering LtdJob No: PVE-3602 Sample 13 Vessel Number: Sample 13

    Number: 2 Mark Number: S2

    Date Printed: 11/12/2009

    Cylindrical Shell Design Information

    Design Pressure: 250.00 PSI Design Temperature: 550 FStatic Head: 17.00 PSI Long. Joint Efficiency: 85 %

    Shell Material: SA-516 Gr. 70 Factor B Chart: CS-2Material Condition: Normalized Material Stress (hot): 19700 PSI

    Shell Length: 88.0000 in. Material Stress (cold): 20000 PSICompressive Stress: 10819 PSI

    Corrosion Allowance: 0.1250 in. Actual Circumferential Stress: 19075 PSIExternal Corrosion Allowance: 0.0000 in. Actual Longitudinal Stress: 9380 PSI

    Outside Diameter (new): 122.2500 in.Outside Diameter (corroded): 122.2500 in. Specific Gravity: 1.00

    Shell Surface Area: 234.70 Sq. Ft. Weight of Fluid: 35997.33 lb.Shell Estimated Volume: 4308.96 Gal. Total Flooded Shell Weight: 46545.50 lb.

    Circ. Joint Efficiency: 85 % Shell Weight: 10548.16 lb.

    Minimum Design Metal Temperature Data

    Min. Temperature Curve: D Pressure at MDMT: 250.00 PSIUCS-66(b) reduction: No Minimum Design Metal Temperature: -20 FUCS-68(c) reduction: No Computed Minimum Temperature: -26 F

    External Pressure Data

    Design Pressure (Pa): 15.00 PSI Design Temperature: 550 F

    Dimension L: 294.0000 in.Ext. Minimum t: 0.6939 in. Ext. Nominal t: 1.1250 in.Minimum L/Do: 2.4049 Nominal L/Do: 2.4049Minimum Do/t: 214.8880 Nominal Do/t: 122.2500

    Minimum Factor A:0.0001862 Nominal Factor A:0.0004285Minimum Factor B: 2418 PSI Nominal Factor B: 5573 PSI

    Design Thickness Calculations

    Longitudinal Stress Calculations per Paragraph UG-27(c)(2)

    t =PR

    2SE + 0.4P=

    267.00 * 60.1250

    2 * 19700 * 0.85 + 0.4 * 267.00= 0.4778 + 0.1250 (corrosion) + 0.0000 (ext.corrosion) = minimum of 0.6028

    Circumferential Stress Calculations per Appendix 1-1(a)(1)

    t =PRo

    SE + 0.4P=

    267.00 * 61.1250

    19700 * 0.85 + 0.4 * 267.00= 0.9685 + 0.1250 (corrosion) + 0.0000 (ext.corrosion) = minimum of 1.0935

    Maximum External Pressure Calculation per Paragraph UG-28

    Pa (using nominalt) =4B

    3(Do / t)=

    4 * 5573

    3 * ( 122.2500 / 1.0000 )= maximum external pressure of 60.78 P

    Extreme Fiber Elongation Calculation per Paragraph UCS-79

    Elongation =50t

    Rf=

    50 * 1.1250

    60.5625= elongation of 0.93

    External loads do not control design.

    Advanced Pressure Vessel version: 10.1.5 Computer Engineering, Inc. Section VIII, Division 1, 2007 Edition, 2008 AddenPage 3 of 95

  • 8/2/2019 Sample13 Spreadsheet

    8/100

    Pressure Vessel Engineering, Ltd.Shell 2

    Job No: PVE-3602 Sample 13 Vessel Number: Sample 13Number: 2 Mark Number: S2

    Date Printed: 11/12/2009

    Nominal Shell Thickness Selected = 1.1250 in.

    Advanced Pressure Vessel version: 10.1.5 Computer Engineering, Inc. Section VIII, Division 1, 2007 Edition, 2008 AddenPage 4 of 95

  • 8/2/2019 Sample13 Spreadsheet

    9/100

    Pressure Vessel Engineering, Ltd.Shell 3

    Customer: Pressure Vessel Engineering LtdJob No: PVE-3602 Sample 13 Vessel Number: Sample 13

    Number: 3 Mark Number: S3

    Date Printed: 11/12/2009

    Cylindrical Shell Design Information

    Design Pressure: 250.00 PSI Design Temperature: 550 FStatic Head: 17.00 PSI Long. Joint Efficiency: 85 %

    Shell Material: SA-516 Gr. 70 Factor B Chart: CS-2Material Condition: Normalized Material Stress (hot): 19700 PSI

    Shell Length: 144.0000 in. Material Stress (cold): 20000 PSICompressive Stress: 10819 PSI

    Corrosion Allowance: 0.1250 in. Actual Circumferential Stress: 19075 PSIExternal Corrosion Allowance: 0.0000 in. Actual Longitudinal Stress: 9380 PSI

    Outside Diameter (new): 122.2500 in.Outside Diameter (corroded): 122.2500 in. Specific Gravity: 1.00

    Shell Surface Area: 384.06 Sq. Ft. Weight of Fluid: 58904.73 lb.Shell Estimated Volume: 7051.03 Gal. Total Flooded Shell Weight: 76165.36 lb.

    Circ. Joint Efficiency: 85 % Shell Weight: 17260.63 lb.

    Minimum Design Metal Temperature Data

    Min. Temperature Curve: D Pressure at MDMT: 250.00 PSIUCS-66(b) reduction: No Minimum Design Metal Temperature: -20 FUCS-68(c) reduction: No Computed Minimum Temperature: -26 F

    External Pressure Data

    Design Pressure (Pa): 15.00 PSI Design Temperature: 550 F

    Dimension L: 294.0000 in.Ext. Minimum t: 0.6939 in. Ext. Nominal t: 1.1250 in.Minimum L/Do: 2.4049 Nominal L/Do: 2.4049Minimum Do/t: 214.8880 Nominal Do/t: 122.2500

    Minimum Factor A:0.0001862 Nominal Factor A:0.0004285Minimum Factor B: 2418 PSI Nominal Factor B: 5573 PSI

    Design Thickness Calculations

    Longitudinal Stress Calculations per Paragraph UG-27(c)(2)

    t =PR

    2SE + 0.4P=

    267.00 * 60.1250

    2 * 19700 * 0.85 + 0.4 * 267.00= 0.4778 + 0.1250 (corrosion) + 0.0000 (ext.corrosion) = minimum of 0.6028

    Circumferential Stress Calculations per Appendix 1-1(a)(1)

    t =PRo

    SE + 0.4P=

    267.00 * 61.1250

    19700 * 0.85 + 0.4 * 267.00= 0.9685 + 0.1250 (corrosion) + 0.0000 (ext.corrosion) = minimum of 1.0935

    Maximum External Pressure Calculation per Paragraph UG-28

    Pa (usi