Code:
Code: ASME VIII-1ASME VIII-1 Year:
Year: 20072007 Cust:Cust: Pressure Vessel EngineeringPressure Vessel Engineering Addenda:
Addenda: 20092009 Desc:Desc: Sample Vessel 4Sample Vessel 4 MAWP:
MAWP: 150150 psipsi Dwg:Dwg: Sample 4Sample 4 MEAWP:
MEAWP: 00 psipsi ID:ID: Sample 4Sample 4 Max. Temp.:
Max. Temp.: 120120 °F°F MDMT:
MDMT: -20-20 °F°F MDMT Press.:
MDMT Press.: 150150 psipsi Min. Thk. (UG-16b):
Min. Thk. (UG-16b): 0.093750.09375 inin Corrosion Allowance:
Corrosion Allowance: 0.1250.125 inin Hydrotest:
Hydrotest: 195195 psipsi Impact Testing:
Impact Testing: NoNo Impact Exemption:
Impact Exemption: UG-20(f)UG-20(f) Radiography:
Radiography: NoneNone
Internal Press.: Internal Press.: YesYes External Press.: External Press.: NoNo
Vessel Weight: Vessel Weight: YesYes Weight of Attachments: Weight of Attachments: NoNo Attachment of Internals: Attachment of Internals: NoNo Attachment of Externals: Attachment of Externals: YesYes Cyclic or Dynamic Reactions: Cyclic or Dynamic Reactions: NoNo
Wind Loading: Wind Loading: NoNo Seismic Loading: Seismic Loading: YesYes Fluid Impact Shock Reactions: Fluid Impact Shock Reactions: NoNo
Temperature Gradients:
Temperature Gradients: NoNo
PVEcalc-Sa
PVEcalc-Sample 4
mple 4 Calulations
Calulations
Differential Thermal Expansion:Differential Thermal Expansion: NoNo Author:Author: Brian MunnBrian Munn Abnormal Pressures:
Abnormal Pressures: NoNo Reviewer:Reviewer: Laurence BrundrettLaurence Brundrett Hydrotest Loads: Hydrotest Loads: NoNo www.pveng.com www.pveng.com [email protected] [email protected] Phone 519-880-9808 Phone 519-880-9808
Pressure Vessel Engineering Ltd. Pressure Vessel Engineering Ltd.
120 Randall Drive, Suite B 120 Randall Drive, Suite B Waterloo, Ontario, Canada, N2V 1C6 Waterloo, Ontario, Canada, N2V 1C6
ASME Calculations - CRN Assistance - Vessel Design - Finite Element Analysis ASME Calculations - CRN Assistance - Vessel Design - Finite Element Analysis
Design Conditions Design Conditions
ASME Section VIII-1 Calculations
ASME Section VIII-1 Calculations
UG-22 Loadings Considered UG-22 Loadings Considered
Conclusion
Conclusion: : The sample vessel The sample vessel has been has been calculatedcalculated to ASME Section VIII-1 and found
0 0 Datum Datum 50 50 100 100 150 150 in in April 15, 2010 April 15, 2010 20 20 120 in x 59 in id 120 in x 59 in id 30 30 30 30
Cover
Cover Page Page 11
Title
Title Page Page 22
Warnings
Warnings and and Errors Errors : : 33
Input
Input Echo Echo : : 44
XY
XY Coordinate Coordinate Calculations Calculations : : 99 Internal
Internal Pressure Pressure Calculations Calculations : : 1010 External
External Pressure Pressure Calculations Calculations : : 1515 Element
Element and and Detail Detail Weights Weights : : 1717 Nozzle
Nozzle Flange Flange MAWP MAWP : : 1919
Natural
Natural Frequency Frequency Calculation Calculation : : 2020 Earthquake
Earthquake Load Load Calculation Calculation : : 2121 Wind/Earthquake
Wind/Earthquake Shear, Shear, Bending Bending : : 2323 Longitudinal
Longitudinal Stress Stress Constants Constants : : 2424 Longitudinal
Longitudinal Allowable Allowable Stresses Stresses : : 2525 Longitudinal
Longitudinal Stresses Stresses Due Due to to . . . . 2626 Stress
Stress due due to to Combined Combined Loads Loads : : 2828 Center
Center of of Gravity Gravity Calculation Calculation : : 3232 Leg
Leg Check, Check, (Operating (Operating Case) Case) : : 3333 Leg
Leg Check, Check, (Filled (Filled w/Water) w/Water) : : 3535 Nozzle
Nozzle Calcs. Calcs. : : N2 N2 3737
Nozzle
Nozzle Calcs. Calcs. : : M2 M2 4141
Nozzle
Nozzle Calcs. Calcs. : : N1 N1 4545
Nozzle
Nozzle Calcs. Calcs. : : M1 M1 4949
Nozzle
Nozzle Calcs. Calcs. : : N3 N3 5454
Nozzle
Nozzle Schedule Schedule : : 5858
Nozzle
Nozzle Summary Summary : : 5959
MDMT
MDMT Summary Summary : : 6060
Vessel
DESIGN CALCULATION DESIGN CALCULATION
In Accordance with ASME Section VIII Division 1 In Accordance with ASME Section VIII Division 1 ASME
ASME Code Code Version Version : : 2007, 2007, Addenda Addenda A-08A-08 Analysis Performed by : PRESSURE VESSEL
Analysis Performed by : PRESSURE VESSEL ENGINEERINGENGINEERING Job
Job File File : : L:\SAMPLES\SAMPLE L:\SAMPLES\SAMPLE 4-VERTICAL 4-VERTICAL VESSEL\SAMPLE VESSEL\SAMPLE 4.1.P4.1.P Date
Date of of Analysis Analysis : : Apr Apr 15,201015,2010 PV
FileName
FileName : : Sample Sample 4.1 4.1 --- --- Page Page 3 3 of of 6262 Warnings
Warnings and and Errors Errors : : Step: Step: 0 0 8:15a 8:15a Apr Apr 15,201015,2010
Class From To : Basic Element Checks. Class From To : Basic Element Checks.
========================================================================== ========================================================================== Note
Note 10 10 20 20 The The wind wind load load will will not not be be computed computed on on this this element.element. Note
Note 20 20 30 30 The The wind wind load load will will not not be be computed computed on on this this element.element. Note
Note 30 30 40 40 The The wind wind load load will will not not be be computed computed on on this this element.element. Class From To: Check of Additional Element Data
Class From To: Check of Additional Element Data
========================================================================== ========================================================================== Warn
Warn 10 10 20 20 Check Check UG-32(j) UG-32(j) and and UG-81 UG-81 for for Crown Crown Radius Radius > > ODOD Warn
Warn 30 30 40 40 Check Check UG-32(j) UG-32(j) and and UG-81 UG-81 for for Crown Crown Radius Radius > > ODOD
PVElite is a registered trademark of COADE, Inc. [2009]
FileName
FileName : : Sample Sample 4.1 4.1 --- --- Page Page 4 4 of of 6262 Input
Input Echo Echo : : Step: Step: 1 1 8:15a 8:15a Apr Apr 15,201015,2010
PV Elite Vessel Analysis Program: Input Data PV Elite Vessel Analysis Program: Input Data
Design
Design Internal Internal Pressure Pressure (for (for Hydrotest) Hydrotest) 150.00 150.00 psigpsig Design
Design Internal Internal Temperature Temperature 120 120 FF Type
Type of of Hydrotest Hydrotest UG99-bUG99-b Hydrotest
Hydrotest Position Position VerticalVertical Projection
Projection of of Nozzle Nozzle from from Vessel Vessel Top Top 0.0000 0.0000 inin Projection
Projection of of Nozzle Nozzle from from Vessel Vessel Bottom Bottom 0.0000 0.0000 inin Minimum
Minimum Design Design Metal Metal Temperature Temperature -20 -20 FF Type
Type of of Construction Construction WeldedWelded Special
Special Service Service NoneNone
Degree
Degree of of Radiography Radiography NoneNone Miscellaneous
Miscellaneous Weight Weight Percent Percent 0.0. Use
Use Higher Higher Longitudinal Longitudinal Stresses Stresses (Flag) (Flag) NN Select
Select t t for for Internal Internal Pressure Pressure (Flag) (Flag) NN Select
Select t t for for External External Pressure Pressure (Flag) (Flag) NN Select
Select t t for for Axial Axial Stress Stress (Flag) (Flag) NN Select
Select Location Location for for Stiff. Stiff. Rings Rings (Flag) (Flag) NN Consider
Consider Vortex Vortex Shedding Shedding NN Perform
Perform a a Corroded Corroded Hydrotest Hydrotest NN Is
Is this this a a Heat Heat Exchanger Exchanger NoNo User
User Defined Defined Hydro. Hydro. Press. Press. (Used (Used if if > > 0) 0) 0.0000 0.0000 psigpsig User
User defined defined MAWP MAWP 0.0000 0.0000 psigpsig User
User defined defined MAPnc MAPnc 0.0000 0.0000 psigpsig Load
Load Case Case 1 1 NP+EW+WI+FW+BWNP+EW+WI+FW+BW Load
Load Case Case 2 2 NP+EW+EE+FS+BSNP+EW+EE+FS+BS Load
Load Case Case 3 3 NP+OW+WI+FW+BWNP+OW+WI+FW+BW Load
Load Case Case 4 4 NP+OW+EQ+FS+BSNP+OW+EQ+FS+BS Load
Load Case Case 5 5 NP+HW+HINP+HW+HI
Load
Load Case Case 6 6 NP+HW+HENP+HW+HE
Load
Load Case Case 7 7 IP+OW+WI+FW+BWIP+OW+WI+FW+BW Load
Load Case Case 8 8 IP+OW+EQ+FS+BSIP+OW+EQ+FS+BS Load
Load Case Case 9 9 EP+OW+WI+FW+BWEP+OW+WI+FW+BW Load
Load Case Case 10 10 EP+OW+EQ+FS+BSEP+OW+EQ+FS+BS Load
Load Case Case 11 11 HP+HW+HIHP+HW+HI Load
Load Case Case 12 12 HP+HW+HEHP+HW+HE Load
Load Case Case 13 13 IP+WE+EWIP+WE+EW Load
Load Case Case 14 14 IP+WF+CWIP+WF+CW Load
Load Case Case 15 15 IP+VO+OWIP+VO+OW Load
Load Case Case 16 16 IP+VE+OWIP+VE+OW Load
Load Case Case 17 17 IP+VF+CWIP+VF+CW Load
Load Case Case 18 18 FS+BS+IP+OWFS+BS+IP+OW Load
Load Case Case 19 19 FS+BS+EP+OWFS+BS+EP+OW Wind
Wind Design Design Code Code No No Wind Wind LoadsLoads Seismic
Seismic Design Design Code Code IBC IBC 20002000 Importance
Importance Factor Factor 1.0001.000
Table
Table Value Value Fa Fa 1.2001.200
Table
Table Value Value Fv Fv 2.8002.800
Short
Short Period Period Acceleration Acceleration value value Ss Ss 0.7500.750 Long
Long Period Period Acceleration Acceleration Value Value Sl Sl 0.3000.300 Moment
Moment Reduction Reduction Factor Factor Tau Tau 1.0001.000 Force
Force Modification Modification Factor Factor R R 2.0002.000 Site
Site Class Class EE
Component
FileName
FileName : : Sample Sample 4.1 4.1 --- --- Page Page 5 5 of of 6262 Input
Input Echo Echo : : Step: Step: 1 1 8:15a 8:15a Apr Apr 15,201015,2010 Amplification
Amplification Factor Factor Ap Ap 0.0000.000 Force
Force Factor Factor 0.0000.000
Consider
Consider Vertical Vertical Acceleration Acceleration NoNo Minimum
Minimum Acceleration Acceleration Multiplier Multiplier 0.0000.000 User
User Value Value of of Sds Sds (used (used if if > > 0 0 ) ) 0.0000.000 User
User Value Value of of Sd1 Sd1 (used (used if if > > 0 0 ) ) 0.0000.000 Design
Design Nozzle Nozzle for for Des. Des. Press. Press. + + St. St. Head Head YY Consider
Consider MAP MAP New New and and Cold Cold in in Noz. Noz. Design Design NN Consider
Consider External External Loads Loads for for Nozzle Nozzle Des. Des. YY Use
Use ASME ASME VIII-1 VIII-1 Appendix Appendix 1-9 1-9 NN Material
Material Database Database Year Year Current Current w/Addenda w/Addenda or or Code Code YearYear
Complete Listing of Vessel Elements and Details: Complete Listing of Vessel Elements and Details:
Element
Element From From Node Node 1010
Element
Element To To Node Node 2020
Element
Element Type Type Torisphe.Torisphe.
Description
Description Bottom Bottom HeadHead
Distance
Distance "FROM" "FROM" to to "TO" "TO" 1.5000 1.5000 inin Element
Element Outside Outside Diameter Diameter 60.000 60.000 inin Element
Element Thickness Thickness 0.6750 0.6750 inin Internal
Internal Corrosion Corrosion Allowance Allowance 0.1250 0.1250 inin Nominal
Nominal Thickness Thickness 0.7500 0.7500 inin External
External Corrosion Corrosion Allowance Allowance 0.0000 0.0000 inin Design
Design Internal Internal Pressure Pressure 150.00 150.00 psigpsig Design
Design Temperature Temperature Internal Internal Pressure Pressure 120 120 FF Design
Design External External Pressure Pressure 0.0000 0.0000 psigpsig Design
Design Temperature Temperature External External Pressure Pressure 70 70 FF Effective
Effective Diameter Diameter Multiplier Multiplier 0.0. Material
Material Name Name SA-516 SA-516 7070 Allowable
Allowable Stress, Stress, Ambient Ambient 20000. 20000. psipsi Allowable
Allowable Stress, Stress, Operating Operating 20000. 20000. psipsi Allowable
Allowable Stress, Stress, Hydrotest Hydrotest 26000. 26000. psipsi Material
Material Density Density 0.2830 0.2830 lbm/in³lbm/in³ P
P Number Number Thickness Thickness 1.2500 1.2500 inin Yield
Yield Stress, Stress, Operating Operating 37080. 37080. psipsi UCS-66
UCS-66 Chart Chart Curve Curve Designation Designation BB External
External Pressure Pressure Chart Chart Name Name CS-2CS-2 UNS
UNS Number Number K02700K02700
Product
Product Form Form PlatePlate
Efficiency,
Efficiency, Longitudinal Longitudinal Seam Seam 0.850.85 Efficiency,
Efficiency, Circumferential Circumferential Seam Seam 0.70.7 Tori
Tori Head Head Crown Crown Radius Radius 60.000 60.000 inin Tori
Tori Head Head Knuckle Knuckle Radius Radius 3.6000 3.6000 inin Element
Element From From Node Node 1010
Detail
Detail Type Type LiquidLiquid
Detail
Detail ID ID BOTTOM BOTTOM HEADHEAD Dist.
Dist. from from "FROM" "FROM" Node Node / / Offset Offset dist dist -10.212 in-10.212 in Height/Length
Height/Length of of Liquid Liquid 11.712 11.712 inin Liquid
Liquid Density Density 62.400 62.400 lbm/ft³lbm/ft³ Element
Element From From Node Node 1010
Detail
Detail Type Type NozzleNozzle
Detail
Detail ID ID N2N2
Dist.
Dist. from from "FROM" "FROM" Node Node / / Offset Offset dist dist 0.0000 0.0000 inin Nozzle
FileName
FileName : : Sample Sample 4.1 4.1 --- --- Page Page 6 6 of of 6262 Input
Input Echo Echo : : Step: Step: 1 1 8:15a 8:15a Apr Apr 15,201015,2010 Nozzle
Nozzle Schedule Schedule 160160
Nozzle
Nozzle Class Class 150150
Layout
Layout Angle Angle 0.0.
Blind
Blind Flange Flange (Y/N) (Y/N) NN Weight
Weight of of Nozzle Nozzle ( ( Used Used if if > > 0 0 ) ) 0.0000 0.0000 lbflbf Grade
Grade of of Attached Attached Flange Flange GR GR 1.11.1 Nozzle
Nozzle Matl Matl SA-106 SA-106 BB
---Element
Element From From Node Node 2020
Element
Element To To Node Node 3030
Element
Element Type Type CylinderCylinder
Description Shell
Description Shell
Distance
Distance "FROM" "FROM" to to "TO" "TO" 120.00 120.00 inin Element
Element Outside Outside Diameter Diameter 60.000 60.000 inin Element
Element Thickness Thickness 0.5000 0.5000 inin Internal
Internal Corrosion Corrosion Allowance Allowance 0.1250 0.1250 inin Nominal
Nominal Thickness Thickness 0.5000 0.5000 inin External
External Corrosion Corrosion Allowance Allowance 0.0000 0.0000 inin Design
Design Internal Internal Pressure Pressure 150.00 150.00 psigpsig Design
Design Temperature Temperature Internal Internal Pressure Pressure 120 120 FF Design
Design External External Pressure Pressure 0.0000 0.0000 psigpsig Design
Design Temperature Temperature External External Pressure Pressure 70 70 FF Effective
Effective Diameter Diameter Multiplier Multiplier 0.0. Material
Material Name Name SA-516 SA-516 7070 Efficiency,
Efficiency, Longitudinal Longitudinal Seam Seam 0.70.7 Efficiency,
Efficiency, Circumferential Circumferential Seam Seam 0.70.7 Element
Element From From Node Node 2020
Detail
Detail Type Type LiquidLiquid
Detail
Detail ID ID SHELLSHELL
Dist.
Dist. from from "FROM" "FROM" Node Node / / Offset Offset dist dist 0.0000 0.0000 inin Height/Length
Height/Length of of Liquid Liquid 120.00 120.00 inin Liquid
Liquid Density Density 62.400 62.400 lbm/ft³lbm/ft³ Element
Element From From Node Node 2020
Detail
Detail Type Type NozzleNozzle
Detail
Detail ID ID M2M2
Dist.
Dist. from from "FROM" "FROM" Node Node / / Offset Offset dist dist 10.000 10.000 inin Nozzle
Nozzle Diameter Diameter 16. 16. in.in. Nozzle
Nozzle Schedule Schedule NoneNone
Nozzle
Nozzle Class Class 00
Layout
Layout Angle Angle 180.180.
Blind
Blind Flange Flange (Y/N) (Y/N) NN Weight
Weight of of Nozzle Nozzle ( ( Used Used if if > > 0 0 ) ) 39.091 39.091 lbflbf Grade
Grade of of Attached Attached Flange Flange NoneNone Nozzle
Nozzle Matl Matl SA-106 SA-106 BB
Element
Element From From Node Node 2020
Detail
Detail Type Type NozzleNozzle
Detail
Detail ID ID N1N1
Dist.
Dist. from from "FROM" "FROM" Node Node / / Offset Offset dist dist 114.00 114.00 inin Nozzle
Nozzle Diameter Diameter 4. 4. in.in. Nozzle
Nozzle Schedule Schedule 160160
Nozzle
Nozzle Class Class 150150
Layout
Layout Angle Angle 0.0.
Blind
Blind Flange Flange (Y/N) (Y/N) NN Weight
FileName
FileName : : Sample Sample 4.1 4.1 --- --- Page Page 7 7 of of 6262 Input
Input Echo Echo : : Step: Step: 1 1 8:15a 8:15a Apr Apr 15,201015,2010 Grade
Grade of of Attached Attached Flange Flange GR GR 1.11.1 Nozzle
Nozzle Matl Matl SA-106 SA-106 BB
Element
Element From From Node Node 2020
Detail
Detail Type Type LegLeg
Detail
Detail ID ID LEGSLEGS
Dist.
Dist. from from "FROM" "FROM" Node Node / / Offset Offset dist dist 12.500 12.500 inin Diameter
Diameter at at Leg Leg Centerline Centerline 60.500 60.500 inin Leg
Leg Orientation Orientation 33
Number
Number of of Legs Legs 44
Section
Section Identifier Identifier W6X15W6X15 Length
Length of of Legs Legs 42.500 42.500 inin
---Element
Element From From Node Node 3030
Element
Element To To Node Node 4040
Element
Element Type Type Torisphe.Torisphe.
Description
Description Top Top HeadHead
Distance
Distance "FROM" "FROM" to to "TO" "TO" 1.5000 1.5000 inin Element
Element Outside Outside Diameter Diameter 60.000 60.000 inin Element
Element Thickness Thickness 0.6750 0.6750 inin Internal
Internal Corrosion Corrosion Allowance Allowance 0.1250 0.1250 inin Nominal
Nominal Thickness Thickness 0.7500 0.7500 inin External
External Corrosion Corrosion Allowance Allowance 0.0000 0.0000 inin Design
Design Internal Internal Pressure Pressure 150.00 150.00 psigpsig Design
Design Temperature Temperature Internal Internal Pressure Pressure 120 120 FF Design
Design External External Pressure Pressure 0.0000 0.0000 psigpsig Design
Design Temperature Temperature External External Pressure Pressure 70 70 FF Effective
Effective Diameter Diameter Multiplier Multiplier 0.0. Material
Material Name Name SA-516 SA-516 7070 Efficiency,
Efficiency, Longitudinal Longitudinal Seam Seam 0.850.85 Efficiency,
Efficiency, Circumferential Circumferential Seam Seam 0.70.7 Tori
Tori Head Head Crown Crown Radius Radius 60.000 60.000 inin Tori
Tori Head Head Knuckle Knuckle Radius Radius 3.6000 3.6000 inin Element
Element From From Node Node 3030
Detail
Detail Type Type LiquidLiquid
Detail
Detail ID ID TOP TOP HEADHEAD
Dist.
Dist. from from "FROM" "FROM" Node Node / / Offset Offset dist dist 0.0000 0.0000 inin Height/Length
Height/Length of of Liquid Liquid 11.462 11.462 inin Liquid
Liquid Density Density 62.400 62.400 lbm/ft³lbm/ft³ Element
Element From From Node Node 3030
Detail
Detail Type Type NozzleNozzle
Detail
Detail ID ID M1M1
Dist.
Dist. from from "FROM" "FROM" Node Node / / Offset Offset dist dist 19.000 19.000 inin Nozzle
Nozzle Diameter Diameter 16. 16. in.in. Nozzle
Nozzle Schedule Schedule NoneNone
Nozzle
Nozzle Class Class 00
Layout
Layout Angle Angle 0.0.
Blind
Blind Flange Flange (Y/N) (Y/N) NN Weight
Weight of of Nozzle Nozzle ( ( Used Used if if > > 0 0 ) ) 0.0000 0.0000 lbflbf Grade
Grade of of Attached Attached Flange Flange NoneNone Nozzle
Nozzle Matl Matl SA-106 SA-106 BB
Element
Element From From Node Node 3030
Detail
Detail Type Type NozzleNozzle
Detail
FileName
FileName : : Sample Sample 4.1 4.1 --- --- Page Page 8 8 of of 6262 Input
Input Echo Echo : : Step: Step: 1 1 8:15a 8:15a Apr Apr 15,201015,2010 Dist.
Dist. from from "FROM" "FROM" Node Node / / Offset Offset dist dist 0.0000 0.0000 inin Nozzle
Nozzle Diameter Diameter 2.25 2.25 in.in. Nozzle
Nozzle Schedule Schedule NoneNone
Nozzle
Nozzle Class Class 00
Layout
Layout Angle Angle 0.0.
Blind
Blind Flange Flange (Y/N) (Y/N) NN Weight
Weight of of Nozzle Nozzle ( ( Used Used if if > > 0 0 ) ) 0.0000 0.0000 lbflbf Grade
Grade of of Attached Attached Flange Flange NoneNone Nozzle
Nozzle Matl Matl SA-105SA-105
PVElite is a registered trademark of COADE, Inc. [2009]
PVElite is a registered trademark of COADE, Inc. [2009]
FileName
FileName : : Sample Sample 4.1 4.1 --- --- Page Page 9 9 of of 6262 XY
XY Coordinate Coordinate Calculations Calculations : : Step: Step: 2 2 8:15a 8:15a Apr Apr 15,201015,2010
XY Coordinate Calculations XY Coordinate Calculations
|
| | | | | | | | | ||
From|
From| To To | | X X (Horiz.)| (Horiz.)| Y Y (Vert.) (Vert.) |DX |DX (Horiz.)| (Horiz.)| DY DY (Vert.) (Vert.) || |
| | | in in | | in in | | in in | | in in || Bottom
Bottom Hea| Hea| 0.00000 0.00000 | | 1.50000 1.50000 | | 0.00000 0.00000 | | 1.50000 1.50000 || Shell|
Shell| 0.00000 0.00000 | | 121.500 121.500 | | 0.00000 0.00000 | | 120.000 120.000 || Top
Top Head| Head| 0.00000 0.00000 | | 123.000 123.000 | | 0.00000 0.00000 | | 1.50000 1.50000 ||
PVElite is a registered trademark of COADE, Inc. [2009]
FileName
FileName : : Sample Sample 4.1 4.1 --- --- Page Page 10 10 of of 6262 Internal
Internal Pressure Pressure Calculations Calculations : : Step: Step: 3 3 8:15a 8:15a Apr Apr 15,201015,2010
Element Thickness, Pressure,
Element Thickness, Pressure, Diameter and AllowDiameter and Allow able Stress :able Stress :
|
| | | Int. Int. Press Press | | Nominal Nominal | | Total Total Corr| Corr| Element Element | | Allowable Allowable || From|
From| To To | | + + Liq. Liq. Hd Hd | | Thickness Thickness | | Allowance Allowance | | Diameter Diameter | | Stress(SE)|Stress(SE)| |
| | | psig psig | | in in | | in in | | in in | | psi psi || Bottom
Bottom Hea| Hea| 155.170 155.170 | | 0.75000 0.75000 | | 0.12500 0.12500 | | 60.0000 60.0000 | | 17000.0 17000.0 || Shell|
Shell| 154.747 154.747 | | 0.50000 0.50000 | | 0.12500 0.12500 | | 60.0000 60.0000 | | 14000.0 14000.0 || Top
Top Head| Head| 150.414 150.414 | | 0.75000 0.75000 | | 0.12500 0.12500 | | 60.0000 60.0000 | | 17000.0 17000.0 ||
Element Required Thickness
Element Required Thickness and MAWP and MAWP ::
|
| | | Design Design | | M.A.W.P. M.A.W.P. | | M.A.P. M.A.P. | | Minimum Minimum | | Required Required || From|
From| To To | | Pressure Pressure | | Corroded Corroded | | New New & & Cold Cold | | Thickness Thickness | | Thickness Thickness || |
| | | psig psig | | psig psig | | psig psig | | in in | | in in || Bottom
Bottom Hea| Hea| 150.000 150.000 | | 171.925 171.925 | | 215.752 215.752 | | 0.67500 0.67500 | | 0.60739 0.60739 || Shell|
Shell| 150.000 150.000 | | 171.132 171.132 | | 234.899 234.899 | | 0.50000 0.50000 | | 0.45514 0.45514 || Top
Top Head| Head| 150.000 150.000 | | 176.735 176.735 | | 215.752 215.752 | | 0.67500 0.67500 | | 0.59254 0.59254 || Minimum
Minimum 171.132 171.132 215.751215.751
MAWP: 171.132 psig, limited by: Shell.
MAWP: 171.132 psig, limited by: Shell.
Internal Pressure Calculation Results : Internal Pressure Calculation Results : AASME Code, Section VIIISME Code, Section VIII , Division 1, 2007 A-08, Division 1, 2007 A-08 Torispherical He
Torispherical He ad From 10 To 20 SA-516 70 , UCS-66 Crv. B at 120 Fad From 10 To 20 SA-516 70 , UCS-66 Crv. B at 120 F
Bottom Head
Bottom Head
LongitudinalLongitudinal Joint: Joint: SeamlessSeamless
Circumferential
Circumferential Joint: Joint: No No Radiography per Radiography per UW UW 11(c) 11(c) Type Type 11
Inside Corroded Head Depth [h]: Inside Corroded Head Depth [h]:
= L - sqrt( ( L - Di / = L - sqrt( ( L - Di / 2) * ( L + Di / 2 - 2) * ( L + Di / 2 - 2 * r ) )2 * r ) ) = = 60.12-sqrt((60.12-60.25/2)*(60.12+60.25/2-2*60.12-sqrt((60.12-60.25/2)*(60.12+60.25/2-2*3.72))3.72)) = 10.285 in = 10.285 in
M factor for Torispherical Heads ( Corroded ):
M factor for Torispherical Heads ( Corroded ):
= (3+sqrt((L+C)/(r+C)))/4 per Appendix 1-4 (b & d) = (3+sqrt((L+C)/(r+C)))/4 per Appendix 1-4 (b & d) = (3+sqrt((60.000 + 0.1250 )/(3.600 + 0.1250 )))/4 = (3+sqrt((60.000 + 0.1250 )/(3.600 + 0.1250 )))/4 = 1.7544
= 1.7544
Required Thickness due to Internal Pressure [tr]: Required Thickness due to Internal Pressure [tr]:
= (P*Lo*M)/(2*S*E+P*(M-0.2)) per Appendix 1-4 (d) = (P*Lo*M)/(2*S*E+P*(M-0.2)) per Appendix 1-4 (d) =
= (155.170*60.6750*1.7544)/(2*20000.00*0.85+15(155.170*60.6750*1.7544)/(2*20000.00*0.85+155.17*(1.7544-0.2))5.17*(1.7544-0.2)) = 0.4824 + 0.1250 = 0.6074 in
= 0.4824 + 0.1250 = 0.6074 in
Max. Allowable Working Pressure at given Thickness, corroded [MAWP]: Max. Allowable Working Pressure at given Thickness, corroded [MAWP]: Less Operating Hydrostatic Head Pressure of 5.170 psig
Less Operating Hydrostatic Head Pressure of 5.170 psig
= (2*S*E*t)/(M*Lo-t*(M-0.2)) per Appendix 1-4 (d) = (2*S*E*t)/(M*Lo-t*(M-0.2)) per Appendix 1-4 (d) =
= (2*20000.00*0.85*0.5500)/(1.7544*60.6750-0.5(2*20000.00*0.85*0.5500)/(1.7544*60.6750-0.5500*(1.75-0.2))500*(1.75-0.2)) =
= 177.095 177.095 - - 5.170 5.170 = = 171.925 171.925 psigpsig
M factor for Torispherical Heads ( New & Cold ):
M factor for Torispherical Heads ( New & Cold ):
= (3+sqrt(L/r))/4 per Appendix 1-4 (b & d) = (3+sqrt(L/r))/4 per Appendix 1-4 (b & d) = (3+sqrt(60.000/3.600))/4
= (3+sqrt(60.000/3.600))/4 = 1.7706
FileName
FileName : : Sample Sample 4.1 4.1 --- --- Page Page 11 11 of of 6262 Internal
Internal Pressure Pressure Calculations Calculations : : Step: Step: 3 3 8:15a 8:15a Apr Apr 15,201015,2010
Maximum Allowable Pressure, New and Cold [MAPNC]: Maximum Allowable Pressure, New and Cold [MAPNC]:
= (2*S*E*t)/(M*Lo - t*(M-0.2)) per Appendix 1-4 (d) = (2*S*E*t)/(M*Lo - t*(M-0.2)) per Appendix 1-4 (d) =
= (2*20000.00*0.85*0.6750)/(1.7706*60.6750-2*0(2*20000.00*0.85*0.6750)/(1.7706*60.6750-2*0.6750*(1.77-0.2)).6750*(1.77-0.2)) = 215.752 psig
= 215.752 psig
Actual stress at given pressure and thickness, corroded [Sact]: Actual stress at given pressure and thickness, corroded [Sact]:
= (P*(M*Lo-t*(M-0.2)))/(2*E*t) = (P*(M*Lo-t*(M-0.2)))/(2*E*t) = = (155.170*(1.7544*60.6750-0.5500*(1.7544-0.2)(155.170*(1.7544*60.6750-0.5500*(1.7544-0.2)))/(2*0.85*0.5500)))/(2*0.85*0.5500) = 17523.934 psi = 17523.934 psi
Straight Flange Required Thickness:
Straight Flange Required Thickness:
=
= (P*Ro)/(S*E+0.4*P) (P*Ro)/(S*E+0.4*P) + + c c per per Appendix Appendix 1-1 1-1 (a)(1)(a)(1) =
= (155.170*30.0000)/(20000.00*0.85+0.4*155.170(155.170*30.0000)/(20000.00*0.85+0.4*155.170)+0.125)+0.125 = 0.398 in
= 0.398 in
Straight Flange Maximum Allowable Working Pressure:
Straight Flange Maximum Allowable Working Pressure:
Less Operating Hydrostatic Head Pressure of 5.170 psigLess Operating Hydrostatic Head Pressure of 5.170 psig
= (S*E*t)/(Ro-0.4*t) per Appendix 1-1 (a)(1) = (S*E*t)/(Ro-0.4*t) per Appendix 1-1 (a)(1)
= (20000.00 * 0.85 * 0.6250 ) / (30.0000 - 0.4 * 0.6250 ) = (20000.00 * 0.85 * 0.6250 ) / (30.0000 - 0.4 * 0.6250 ) =
= 357.143 357.143 - - 5.170 5.170 = = 351.973 351.973 psigpsig Percent
Percent Elongation Elongation per per UCS-79 UCS-79 (75*tnom/Rf)*(1-Rf/Ro) (75*tnom/Rf)*(1-Rf/Ro) 14.151 14.151 %%
Note: Please Check Requirements of UCS-79 as Elongation is > 5%.
Note: Please Check Requirements of UCS-79 as Elongation is > 5%.
MDMT Calculations in the Knuckle Portion:
MDMT Calculations in the Knuckle Portion:
Govrn. thk, tg = 0.675 , tr = 0.482 , c = 0.1250 in , E* = 0.85
Govrn. thk, tg = 0.675 , tr = 0.482 , c = 0.1250 in , E* = 0.85
Stress Ratio = tr * (E*) / (tg - c) = 0.746 , Temp. Reduction = 25 F
Stress Ratio = tr * (E*) / (tg - c) = 0.746 , Temp. Reduction = 25 F
MinMin Metal Metal Temp. Temp. w/o w/o impact impact per per UCS-66 UCS-66 10 10 FF Min
Min Metal Metal Temp. Temp. at at Required Required thickness thickness (UCS (UCS 66.1) 66.1) -15 -15 FF Min
Min Metal Metal Temp. Temp. w/o w/o impact impact per per UG-20(f) UG-20(f) -20 -20 FF
MDMT Calculations in the Head Straight Flange:
MDMT Calculations in the Head Straight Flange:
Govrn. thk, tg = 0.750 , tr = 0.264 , c = 0.1250 in , E* = 0.85
Govrn. thk, tg = 0.750 , tr = 0.264 , c = 0.1250 in , E* = 0.85
Stress Ratio = tr * (E*) / (tg - c) = 0.360 , Temp. Reduction = 130 F
Stress Ratio = tr * (E*) / (tg - c) = 0.360 , Temp. Reduction = 130 F
MinMin Metal Metal Temp. Temp. w/o w/o impact impact per per UCS-66 UCS-66 16 16 FF Min
Min Metal Metal Temp. Temp. at at Required Required thickness thickness (UCS (UCS 66.1) 66.1) -55 -55 FF Min
Min Metal Metal Temp. Temp. w/o w/o impact impact per per UG-20(f) UG-20(f) -20 -20 FF
Cylindrical Shell From 20 To 30 SA-516 70 , UCS-66 Crv.
Cylindrical Shell From 20 To 30 SA-516 70 , UCS-66 Crv. B at 120 B at 120 FF
Shell
Shell
Longitudinal
Longitudinal Joint: Joint: No No Radiography Radiography per per UW UW 11(c) 11(c) Type Type 11
Circumferential
Circumferential Joint: Joint: No No Radiography per Radiography per UW UW 11(c) 11(c) Type Type 11
Required Thickness due to Internal Pressure [tr]: Required Thickness due to Internal Pressure [tr]:
= (P*Ro)/(S*E+0.4*P) per Appendix 1-1 (a)(1) = (P*Ro)/(S*E+0.4*P) per Appendix 1-1 (a)(1) =
= (154.747*30.0000)/(20000.00*0.70+0.4*154.747(154.747*30.0000)/(20000.00*0.70+0.4*154.747)) = 0.3301 + 0.1250 = 0.4551 in
= 0.3301 + 0.1250 = 0.4551 in
Max. Allowable Working Pressure at given Thickness, corroded [MAWP]: Max. Allowable Working Pressure at given Thickness, corroded [MAWP]: Less Operating Hydrostatic Head Pressure of 4.747 psig
Less Operating Hydrostatic Head Pressure of 4.747 psig
= (S*E*t)/(Ro-0.4*t) per Appendix 1-1 (a)(1) = (S*E*t)/(Ro-0.4*t) per Appendix 1-1 (a)(1) = (20000.00*0.70*0.3750)/(30.0000-0.4*0.3750) = (20000.00*0.70*0.3750)/(30.0000-0.4*0.3750) =
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Internal Pressure Pressure Calculations Calculations : : Step: Step: 3 3 8:15a 8:15a Apr Apr 15,201015,2010
Maximum Allowable Pressure, New and Cold [MAPNC]: Maximum Allowable Pressure, New and Cold [MAPNC]:
= (S*E*t)/(Ro-0.4*t) per Appendix 1-1 (a)(1) = (S*E*t)/(Ro-0.4*t) per Appendix 1-1 (a)(1) = (20000.00*0.70*0.5000)/(30.0000-0.4*0.5000) = (20000.00*0.70*0.5000)/(30.0000-0.4*0.5000) = 234.899 psig
= 234.899 psig
Actual stress at given pressure and thickness, corroded [Sact]: Actual stress at given pressure and thickness, corroded [Sact]:
= (P*(Ro-0.4*t))/(E*t) = (P*(Ro-0.4*t))/(E*t) = = (154.747*((30.0000-0.4*0.3750))/(0.70*0.3750(154.747*((30.0000-0.4*0.3750))/(0.70*0.3750)) = 17596.973 psi = 17596.973 psi Percent
Percent Elongation Elongation per per UCS-79 UCS-79 (50*tnom/Rf)*(1-Rf/Ro) (50*tnom/Rf)*(1-Rf/Ro) 0.840 0.840 %%
Minimum Design Metal Temperature Results:
Minimum Design Metal Temperature Results:
Govrn. thk, tg = 0.500 , tr = 0.330 , c = 0.1250 in , E* = 0.80
Govrn. thk, tg = 0.500 , tr = 0.330 , c = 0.1250 in , E* = 0.80
Stress Ratio = tr * (E*) / (tg - c) = 0.704 , Temp. Reduction = 30 F
Stress Ratio = tr * (E*) / (tg - c) = 0.704 , Temp. Reduction = 30 F
MinMin Metal Metal Temp. Temp. w/o w/o impact impact per per UCS-66 UCS-66 -6 -6 FF Min
Min Metal Metal Temp. Temp. at at Required Required thickness thickness (UCS (UCS 66.1) 66.1) -36 -36 FF Min
Min Metal Metal Temp. Temp. w/o w/o impact impact per per UG-20(f) UG-20(f) -20 -20 FF
Torispherical He
Torispherical He ad From 30 To 40 SA-516 70 , UCS-66 Crv. B at 120 Fad From 30 To 40 SA-516 70 , UCS-66 Crv. B at 120 F
Top Head
Top Head
LongitudinalLongitudinal Joint: Joint: SeamlessSeamless
Circumferential
Circumferential Joint: Joint: No No Radiography per Radiography per UW UW 11(c) 11(c) Type Type 11
Inside Corroded Head Depth [h]: Inside Corroded Head Depth [h]:
= L - sqrt( ( L - Di / = L - sqrt( ( L - Di / 2) * ( L + Di / 2 - 2) * ( L + Di / 2 - 2 * r ) )2 * r ) ) = = 60.12-sqrt((60.12-60.25/2)*(60.12+60.25/2-2*60.12-sqrt((60.12-60.25/2)*(60.12+60.25/2-2*3.72))3.72)) = 10.285 in = 10.285 in
M factor for Torispherical Heads ( Corroded ):
M factor for Torispherical Heads ( Corroded ):
= (3+sqrt((L+C)/(r+C)))/4 per Appendix 1-4 (b & d) = (3+sqrt((L+C)/(r+C)))/4 per Appendix 1-4 (b & d) = (3+sqrt((60.000 + 0.1250 )/(3.600 + 0.1250 )))/4 = (3+sqrt((60.000 + 0.1250 )/(3.600 + 0.1250 )))/4 = 1.7544
= 1.7544
Required Thickness due to Internal Pressure [tr]: Required Thickness due to Internal Pressure [tr]:
= (P*Lo*M)/(2*S*E+P*(M-0.2)) per Appendix 1-4 (d) = (P*Lo*M)/(2*S*E+P*(M-0.2)) per Appendix 1-4 (d) =
= (150.360*60.6750*1.7544)/(2*20000.00*0.85+15(150.360*60.6750*1.7544)/(2*20000.00*0.85+150.36*(1.7544-0.2))0.36*(1.7544-0.2)) = 0.4675 + 0.1250 = 0.5925 in
= 0.4675 + 0.1250 = 0.5925 in
Max. Allowable Working Pressure at given Thickness, corroded [MAWP]: Max. Allowable Working Pressure at given Thickness, corroded [MAWP]: Less Operating Hydrostatic Head Pressure of 0.360 psig
Less Operating Hydrostatic Head Pressure of 0.360 psig
= (2*S*E*t)/(M*Lo-t*(M-0.2)) per Appendix 1-4 (d) = (2*S*E*t)/(M*Lo-t*(M-0.2)) per Appendix 1-4 (d) =
= (2*20000.00*0.85*0.5500)/(1.7544*60.6750-0.5(2*20000.00*0.85*0.5500)/(1.7544*60.6750-0.5500*(1.75-0.2))500*(1.75-0.2)) =
= 177.095 177.095 - - 0.360 0.360 = = 176.735 176.735 psigpsig
M factor for Torispherical Heads ( New & Cold ):
M factor for Torispherical Heads ( New & Cold ):
= (3+sqrt(L/r))/4 per Appendix 1-4 (b & d) = (3+sqrt(L/r))/4 per Appendix 1-4 (b & d) = (3+sqrt(60.000/3.600))/4
= (3+sqrt(60.000/3.600))/4 = 1.7706
= 1.7706
Maximum Allowable Pressure, New and Cold [MAPNC]: Maximum Allowable Pressure, New and Cold [MAPNC]:
= (2*S*E*t)/(M*Lo - t*(M-0.2)) per Appendix 1-4 (d) = (2*S*E*t)/(M*Lo - t*(M-0.2)) per Appendix 1-4 (d) =
= (2*20000.00*0.85*0.6750)/(1.7706*60.6750-2*0(2*20000.00*0.85*0.6750)/(1.7706*60.6750-2*0.6750*(1.77-0.2)).6750*(1.77-0.2)) = 215.752 psig
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FileName : : Sample Sample 4.1 4.1 --- --- Page Page 13 13 of of 6262 Internal
Internal Pressure Pressure Calculations Calculations : : Step: Step: 3 3 8:15a 8:15a Apr Apr 15,201015,2010
Actual stress at given pressure and thickness, corroded [Sact]: Actual stress at given pressure and thickness, corroded [Sact]:
= (P*(M*Lo-t*(M-0.2)))/(2*E*t) = (P*(M*Lo-t*(M-0.2)))/(2*E*t) = = (150.360*(1.7544*60.6750-0.5500*(1.7544-0.2)(150.360*(1.7544*60.6750-0.5500*(1.7544-0.2)))/(2*0.85*0.5500)))/(2*0.85*0.5500) = 16980.678 psi = 16980.678 psi
Straight Flange Required Thickness:
Straight Flange Required Thickness:
=
= (P*Ro)/(S*E+0.4*P) (P*Ro)/(S*E+0.4*P) + + c c per per Appendix Appendix 1-1 1-1 (a)(1)(a)(1) =
= (150.360*30.0000)/(20000.00*0.85+0.4*150.360(150.360*30.0000)/(20000.00*0.85+0.4*150.360)+0.125)+0.125 = 0.389 in
= 0.389 in
Straight Flange Maximum Allowable Working Pressure:
Straight Flange Maximum Allowable Working Pressure:
Less Operating Hydrostatic Head Pressure of 0.360 psigLess Operating Hydrostatic Head Pressure of 0.360 psig
= (S*E*t)/(Ro-0.4*t) per Appendix 1-1 (a)(1) = (S*E*t)/(Ro-0.4*t) per Appendix 1-1 (a)(1)
= (20000.00 * 0.85 * 0.6250 ) / (30.0000 - 0.4 * 0.6250 ) = (20000.00 * 0.85 * 0.6250 ) / (30.0000 - 0.4 * 0.6250 ) =
= 357.143 357.143 - - 0.360 0.360 = = 356.783 356.783 psigpsig Percent
Percent Elongation Elongation per per UCS-79 UCS-79 (75*tnom/Rf)*(1-Rf/Ro) (75*tnom/Rf)*(1-Rf/Ro) 14.151 14.151 %%
Note: Please Check Requirements of UCS-79 as Elongation is > 5%.
Note: Please Check Requirements of UCS-79 as Elongation is > 5%.
MDMT Calculations in the Knuckle Portion:
MDMT Calculations in the Knuckle Portion:
Govrn. thk, tg = 0.675 , tr = 0.468 , c = 0.1250 in , E* = 0.85
Govrn. thk, tg = 0.675 , tr = 0.468 , c = 0.1250 in , E* = 0.85
Stress Ratio = tr * (E*) / (tg - c) = 0.723 , Temp. Reduction = 28 F
Stress Ratio = tr * (E*) / (tg - c) = 0.723 , Temp. Reduction = 28 F
MinMin Metal Metal Temp. Temp. w/o w/o impact impact per per UCS-66 UCS-66 10 10 FF Min
Min Metal Metal Temp. Temp. at at Required Required thickness thickness (UCS (UCS 66.1) 66.1) -17 -17 FF Min
Min Metal Metal Temp. Temp. w/o w/o impact impact per per UG-20(f) UG-20(f) -20 -20 FF
MDMT Calculations in the Head Straight Flange:
MDMT Calculations in the Head Straight Flange:
Govrn. thk, tg = 0.750 , tr = 0.264 , c = 0.1250 in , E* = 0.85
Govrn. thk, tg = 0.750 , tr = 0.264 , c = 0.1250 in , E* = 0.85
Stress Ratio = tr * (E*) / (tg - c) = 0.360 , Temp. Reduction = 130 F
Stress Ratio = tr * (E*) / (tg - c) = 0.360 , Temp. Reduction = 130 F
MinMin Metal Metal Temp. Temp. w/o w/o impact impact per per UCS-66 UCS-66 16 16 FF Min
Min Metal Metal Temp. Temp. at at Required Required thickness thickness (UCS (UCS 66.1) 66.1) -55 -55 FF Min
Min Metal Metal Temp. Temp. w/o w/o impact impact per per UG-20(f) UG-20(f) -20 -20 FF
Note: Heads and Shells Exempted to -20F (-29C) by paragraph UG-20F
Note: Heads and Shells Exempted to -20F (-29C) by paragraph UG-20F
Hydrostatic Test Pressure Results: Hydrostatic Test Pressure Results:
Pressure
Pressure per per UG99b UG99b = = 1.3 1.3 * * M.A.W.P. M.A.W.P. * * Sa/S Sa/S 222.472 222.472 psigpsig Pressure
Pressure per per UG99b[34] UG99b[34] = = 1.3 1.3 * * Design Design Pres Pres * * Sa/S Sa/S 195.000 195.000 psigpsig Pressure
Pressure per per UG99c UG99c = = 1.3 1.3 * * M.A.P. M.A.P. - - Head(Hyd) Head(Hyd) 275.327 psig275.327 psig Pressure
Pressure per per UG100 UG100 = = 1.1 1.1 * * M.A.W.P. M.A.W.P. * * Sa/S Sa/S 188.245 188.245 psigpsig
Vertical Test performed per: UG-99b Vertical Test performed per: UG-99b
Stresses on Elements due
Stresses on Elements due to Hydrostatic Test Pressure:to Hydrostatic Test Pressure:
From
From To To Stress Stress Allowable Allowable Ratio Ratio PressurePressure Bottom
Bottom Head Head 21100.3 21100.3 26000.0 26000.0 0.812 0.812 227.62227.62 Shell
Shell 19345.6 19345.6 26000.0 26000.0 0.744 0.744 227.21227.21 Top
Top Head Head 20660.8 20660.8 26000.0 26000.0 0.795 0.795 222.88222.88
Elements Suitable for Internal Pressure.
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FileName : : Sample Sample 4.1 4.1 --- --- Page Page 14 14 of of 6262 Internal
Internal Pressure Pressure Calculations Calculations : : Step: Step: 3 3 8:15a 8:15a Apr Apr 15,201015,2010
PVElite is a registered trademark of COADE, Inc. [2009]
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FileName : : Sample Sample 4.1 4.1 --- --- Page Page 15 15 of of 6262 External
External Pressure Pressure Calculations Calculations : : Step: Step: 4 4 8:15a 8:15a Apr Apr 15,201015,2010
External Pressure Calculation Results : External Pressure Calculation Results : A
ASME Code, Section VIIISME Code, Section VIII , Division 1, 2007 A-08, Division 1, 2007 A-08 Toris
Torispherical Head From 10 pherical Head From 10 to 20 Ext. Chart: CS-2 at 70 Fto 20 Ext. Chart: CS-2 at 70 F
Bottom Head
Bottom Head
Elastic Modulus
Elastic Modulus from C
from Chart: C
hart: CS-2
S-2 at 70
at 70 F
F :
: 0.29000E+08
0.29000E+08 psi
psi
Results for Maximum Allowable External Pressure (MAEP):
Results for Maximum Allowable External Pressure (MAEP):
Tca
Tca Sph. Sph. Rad Rad Ro/t Ro/t Factor Factor A A BB 0.550
0.550 60.67 60.67 110.32 110.32 0.0011331 0.0011331 12914.9612914.96 EMAP = B/(Ro/t) = 12914.9561 /110.3182 = 117.0701 psig EMAP = B/(Ro/t) = 12914.9561 /110.3182 = 117.0701 psig
Cylindrical Shell From 20
Cylindrical Shell From 20 to 30 Extto 30 Ext . Chart: . Chart: CS-2 at 70 FCS-2 at 70 F
Shell
Shell
Elastic Modulus
Elastic Modulus from C
from Chart: C
hart: CS-2
S-2 at 70
at 70 F
F :
: 0.29000E+08
0.29000E+08 psi
psi
Results for Maximum Allowable External Pressure (MAEP):
Results for Maximum Allowable External Pressure (MAEP):
Tca
Tca OD OD SLEN SLEN D/t D/t L/D L/D Factor Factor A A BB 0.375
0.375 60.00 60.00 129.54 129.54 160.00 160.00 2.1590 2.1590 0.0003025 0.0003025 4386.304386.30 EMAP = (4*B)/(3*(D/t)) = (4*4386.2959 )/(3*160.0000 ) = 36.5525 psig EMAP = (4*B)/(3*(D/t)) = (4*4386.2959 )/(3*160.0000 ) = 36.5525 psig
Results for Maximum Stiffened Length (Slen):
Results for Maximum Stiffened Length (Slen):
TcaTca OD OD SLEN SLEN D/t D/t L/D L/D Factor Factor A A BB 0.375
0.375 60.00 60.00 0.33E+33 0.33E+33 160.00 160.00 .5000E+02 .5000E+02 0.0000430 0.0000430 623.05623.05 EMAP = (4*B)/(3*(D/t)) = (4*623.0469 )/(3*160.0000 ) = 5.1921 psig EMAP = (4*B)/(3*(D/t)) = (4*623.0469 )/(3*160.0000 ) = 5.1921 psig
Toris
Torispherical Head From 30 pherical Head From 30 to 40 Ext. Chart: CS-2 at 70 Fto 40 Ext. Chart: CS-2 at 70 F
Top Head
Top Head
Elastic Modulus
Elastic Modulus from C
from Chart: C
hart: CS-2
S-2 at 70
at 70 F
F :
: 0.29000E+08
0.29000E+08 psi
psi
Results for Maximum Allowable External Pressure (MAEP):
Results for Maximum Allowable External Pressure (MAEP):
Tca
Tca Sph. Sph. Rad Rad Ro/t Ro/t Factor Factor A A BB 0.550
0.550 60.67 60.67 110.32 110.32 0.0011331 0.0011331 12914.9612914.96 EMAP = B/(Ro/t) = 12914.9561 /110.3182 = 117.0701 psig EMAP = B/(Ro/t) = 12914.9561 /110.3182 = 117.0701 psig
External Pressure Calculations External Pressure Calculations
|
| | | Section Section | | Outside Outside | | Corroded Corroded | | Factor Factor | | Factor Factor || From|
From| To To | | Length Length | | Diameter Diameter | | Thickness Thickness | | A A | | B B || | | | | in in | | in in | | in in | | | | psi psi || 10| 20| 10| 20| No No Calc Calc | | 60.6750 60.6750 | | 0.55000 0.55000 | 0.0011331 | 0.0011331 | | 12915.0 12915.0 || 20| 30| 20| 30| 129.539 129.539 | | 60.0000 60.0000 | | 0.37500 0.37500 | | 0.00030250 0.00030250 | | 4386.30 4386.30 || 30| 40| 30| 40| No No Calc Calc | | 60.6750 60.6750 | | 0.55000 0.55000 | 0.0011331 | 0.0011331 | | 12915.0 12915.0 ||
External Pressure Calculations External Pressure Calculations
|
| | | External External | | External External | | External External | | External External || From|
From| To To | | Actual Actual T. T. | | Required Required T.|Des. T.|Des. Press. Press. | | M.A.W.P. M.A.W.P. || |
| | | in in | | in in | | psig psig | | psig psig || 10|
10| 20| 20| 0.67500 0.67500 | | No No Calc Calc | | 0.00000 0.00000 | | 117.070 117.070 || 20|
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External Pressure Pressure Calculations Calculations : : Step: Step: 4 4 8:15a 8:15a Apr Apr 15,201015,2010 30|
30| 40| 40| 0.67500 0.67500 | | No No Calc Calc | | 0.00000 0.00000 | | 117.070 117.070 ||
Minimum 36.552
Minimum 36.552
External Pressure Calculations External Pressure Calculations
|
| | | Actual Actual Len.| Len.| Allow. Allow. Len.| Len.| Ring Ring Inertia Inertia | | Ring Ring Inertia Inertia || From|
From| To To | | Bet. Bet. Stiff.| Stiff.| Bet. Bet. Stiff.| Stiff.| Required Required | | Available Available || |
| | | in in | | in in | | in**4 in**4 | | in**4 in**4 || 10|
10| 20| 20| No No Calc Calc | | No No Calc Calc | | No No Calc Calc | | No No Calc Calc || 20|
20| 30| 30| 129.539 129.539 | | 328.4E+30 328.4E+30 | | No No Calc Calc | | No No Calc Calc || 30|
30| 40| 40| No No Calc Calc | | No No Calc Calc | | No No Calc Calc | | No No Calc Calc ||
Elements Suitable for External Pressure.
Elements Suitable for External Pressure.
PVElite is a registered trademark of COADE, Inc. [2009]
PVElite is a registered trademark of COADE, Inc. [2009]
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FileName : : Sample Sample 4.1 4.1 --- --- Page Page 17 17 of of 6262 Element
Element and and Detail Detail Weights Weights : : Step: Step: 5 5 8:15a 8:15a Apr Apr 15,201015,2010
Element and Detail Weights Element and Detail Weights
|
| | | Element Element | | Element Element | Corroded | Corroded | | Corroded Corroded | | Extra Extra due |due | From|
From| To To | | Metal Metal Wgt. Wgt. | | ID ID Volume Volume |Metal |Metal Wgt. Wgt. | | ID ID Volume Volume | | Misc Misc % % || | | | | lbf lbf | | ft³ ft³ | | lbf lbf | | ft³ ft³ | | lbf lbf || 10| 10| 20| 20| 762.967 762.967 | | 11.7502 11.7502 | | 639.274 639.274 | | 12.0032 12.0032 | | 0.00000 0.00000 || 20| 20| 30| 30| 3173.99 3173.99 | | 189.858 189.858 | | 2385.50 2385.50 | | 191.470 191.470 | | 0.00000 0.00000 || 30| 30| 40| 40| 762.967 762.967 | | 11.7502 11.7502 | | 639.274 639.274 | | 12.0032 12.0032 | | 0.00000 0.00000 || ---Total Total 4699 4699 213 213 3664 3664 215 215 00 Weight of Details Weight of Details |
| | | Weight Weight of of | | X X Offset, Offset, | | Y Y Offset, Offset, || From|Type|
From|Type| Detail Detail | | Dtl. Dtl. Cent. Cent. |Dtl. |Dtl. Cent. Cent. | | DescriptionDescription |
| | | lbf lbf | | in in | | in in || 10|Liqd|
10|Liqd| 811.588 811.588 | | 0.00000 0.00000 | -| -5.10578 5.10578 | | BOTTOM BOTTOM HEADHEAD 10|Nozl|
10|Nozl| 16.3337 16.3337 | | 0.00000 0.00000 | | 0.81738 0.81738 | | N2N2 20|Liqd|
20|Liqd| 11847.2 11847.2 | | 0.00000 0.00000 | | 60.0000 60.0000 | | SHELLSHELL 20|Nozl|
20|Nozl| 39.0913 39.0913 | | 37.5000 37.5000 | | 10.0000 10.0000 | | M2M2 20|Nozl|
20|Nozl| 11.0755 11.0755 | | 31.5000 31.5000 | | 114.000 114.000 | | N1N1 20|Legs|
20|Legs| 254.730 254.730 | | 0.00000 0.00000 | | -8.74980 -8.74980 | | LEGSLEGS 30|Liqd|
30|Liqd| 734.315 734.315 | | 0.00000 0.00000 | | 4.98101 4.98101 | | TOP TOP HEADHEAD 30|Nozl|
30|Nozl| 42.4670 42.4670 | | 0.00000 0.00000 | | 0.81738 0.81738 | | M1M1 30|Nozl|
30|Nozl| 1.25949 1.25949 | | 0.00000 0.00000 | | 0.81738 0.81738 | | N3N3
Total Weight of Each Detail Type Total Weight of Each Detail Type
Total
Total Weight Weight of of Liquid Liquid 13393.113393.1 Total
Total Weight Weight of of Nozzles Nozzles 110.2110.2 Total
Total Weight Weight of of Legs Legs 254.7254.7
---Sum
Sum of of the the Detail Detail Weights Weights 13758.1 13758.1 lbflbf
Weight Summary
Weight Summary
FabricatedFabricated Wt. Wt. - - Bare Bare Weight Weight W/O W/O Removable Removable Internals Internals 5064.9 5064.9 lbflbf Shop
Shop Test Test Wt. Wt. - - Fabricated Fabricated Weight Weight + + Water Water ( ( Full Full ) ) 18378.5 18378.5 lbflbf Shipping
Shipping Wt. Wt. - - Fab. Fab. Wt Wt + + Rem. Rem. Intls.+ Intls.+ Shipping Shipping App. App. 5064.9 5064.9 lbflbf Erected Wt.
Erected Wt. - - Fab. Fab. Wt Wt + + Rem. Rem. Intls.+ Intls.+ Insul. Insul. (etc) (etc) 5064.9 5064.9 lbflbf Ope.
Ope. Wt. Wt. no no Liq Liq - - Fab. Fab. Wt Wt + + Intls. Intls. + + Details Details + + Wghts. Wghts. 5064.9 5064.9 lbflbf Operating
Operating Wt. Wt. - - Empty Empty Wt. Wt. + + Operating Operating Liquid Liquid (No (No CA) CA) 18458.0 18458.0 lbflbf Field
Field Test Test Wt. Wt. - - Empty Empty Weight Weight + + Water Water (Full) (Full) 18378.5 18378.5 lbflbf Mass
Mass of of the the Upper Upper 1/3 1/3 of of the the Vertical Vertical Vessel Vessel 6113.3 6113.3 lbflbf
Outside Surface Areas of Elements Outside Surface Areas of Elements
|
| | | Surface Surface || From|
From| To To | | Area Area || | | | | in² in² || 10| 10| 20| 20| 3630.95 3630.95 || 20| 20| 30| 30| 22619.5 22619.5 || 30| 30| 40| 40| 3630.95 3630.95 || ---Total
Total 29881.373 29881.373 in² in² [207.5 [207.5 Square Square Feet Feet ]]
Element and Detail Weights Element and Detail Weights
FileName
FileName : : Sample Sample 4.1 4.1 --- --- Page Page 18 18 of of 6262 Element
Element and and Detail Detail Weights Weights : : Step: Step: 5 5 8:15a 8:15a Apr Apr 15,201015,2010 |
| To To | | Total Total Ele.| Ele.| Total. Total. Ele.|Total. Ele.|Total. Ele.| Ele.| Total Total Dtl.| Dtl.| Oper. Oper. Wgt. Wgt. || From|
From| To To | | Empty Empty Wgt.| Wgt.| Oper. Oper. Wgt.|Hydro. Wgt.|Hydro. Wgt.| Wgt.| Offset Offset Mom.| Mom.| No No Liquid Liquid || | | | | lbm lbm | | lbm lbm | | lbm lbm | | in-lb in-lb | | lbm lbm || 10| 10| 20| 20| 779.301 779.301 | | 1590.89 1590.89 | | 1512.52 1512.52 | | 0.00000 0.00000 | | 779.301 779.301 || 20|Legs| 20|Legs| 335.860 335.860 | | 1569.98 1569.98 | | 1569.98 1569.98 | | 189.048 189.048 | | 335.860 335.860 || Legs| Legs| 30| 30| 2888.29 2888.29 | | 13501.4 13501.4 | | 13501.4 13501.4 | | 1625.75 1625.75 | | 2888.29 2888.29 || 30| 30| 40| 40| 806.694 806.694 | | 1541.01 1541.01 | | 1539.91 1539.91 | | 0.00000 0.00000 | | 806.694 806.694 ||
Cumulative Vessel Weight Cumulative Vessel Weight
|
| | | Cumulative Cumulative Ope Ope | | Cumulative Cumulative | | Cumulative Cumulative || From| To | Wgt. No Liquid | Oper. Wgt. | Hydro. Wgt. | From| To | Wgt. No Liquid | Oper. Wgt. | Hydro. Wgt. |
| | | | lbm lbm | | lbm lbm | | llbm bm || 10| 10| 20| 20| -779.301 -779.301 | | -1590.89 -1590.89 | | -1512.52 -1512.52 || 20|Legs| 20|Legs| -1115.16 -1115.16 | | -3160.87 | -3160.87 | -3082.50 -3082.50 || Legs| Legs| 30| 30| 3694.99 3694.99 | | 15042.4 15042.4 | | 15041.3 15041.3 || 30| 30| 40| 40| 806.694 806.694 | | 1541.01 1541.01 | | 1539.91 1539.91 ||
Note: The cumulative operating weights no liquid in the column above
Note: The cumulative operating weights no liquid in the column above
are the cumulative operating weights minus the operating liquid
are the cumulative operating weights minus the operating liquid
weight minus any weights absent in the empty condition.
weight minus any weights absent in the empty condition.
Cumulative Vessel MomentCumulative Vessel Moment
|
| | | Cumulative Cumulative | | Cumulative Cumulative |Cumulative |Cumulative || From| To | Empty Mom. | Oper. Mom. |Hydro. Mom.| From| To | Empty Mom. | Oper. Mom. |Hydro. Mom.|
|
| | | in-lb in-lb | | in-lb in-lb | | in-lb in-lb || 10| 10| 20| 20| 0.00000 0.00000 | | 0.00000 0.00000 | | 0.00000 0.00000 || 20|Legs| 20|Legs| 189.048 189.048 | | 189.048 189.048 | | 189.048 189.048 || Legs| Legs| 30| 30| 1625.75 1625.75 | | 1625.75 1625.75 | | 1625.75 1625.75 || 30| 30| 40| 40| 0.00000 0.00000 | | 0.00000 0.00000 | | 0.00000 0.00000 ||
PVElite is a registered trademark of COADE, Inc. [2009]
FileName
FileName : : Sample Sample 4.1 4.1 --- --- Page Page 19 19 of of 6262 Nozzle
Nozzle Flange Flange MAWP MAWP : : Step: Step: 6 6 8:15a 8:15a Apr Apr 15,201015,2010
Nozzle Flange MAWP Results : Nozzle Flange MAWP Results :
Nozzle
Nozzle --- --- Flange Flange RatingRating Description
Description Operating Operating Ambient Ambient Temperature Temperature Class Class Grade|GroupGrade|Group psig
psig psig psig FF
---N2 N2 280.0 280.0 285.0 285.0 120 120 150 150 GR GR 1.11.1 N1 N1 280.0 280.0 285.0 285.0 120 120 150 150 GR GR 1.11.1 ---Minimum
Minimum Rating Rating 280.000 280.000 285.000 285.000 psigpsig
Note: ANSI Ratings are per ANSI/ASME B16.5 2003 Edition
Note: ANSI Ratings are per ANSI/ASME B16.5 2003 Edition
PVElite is a registered trademark of COADE, Inc. [2009]
PVElite is a registered trademark of COADE, Inc. [2009]
FileName
FileName : : Sample Sample 4.1 4.1 --- --- Page Page 20 20 of of 6262 Natural
Natural Frequency Frequency Calculation Calculation : : Step: Step: 7 7 8:15a 8:15a Apr Apr 15,201015,2010
The Natural Frequencies for the vessel have been computed iteratively
The Natural Frequencies for the vessel have been computed iteratively
by solving a
by solving a
system of matrices.
system of matrices.
These matrices describe the
These matrices describe the
mass
mass
and the
and the
stiffness of the vessel.
stiffness of the vessel.
This is the gen
This is the gen
eralized eigenvalue/
eralized eigenvalue/
eigenvector problem and is referenced in some mathematical texts.
eigenvector problem and is referenced in some mathematical texts.
The Natural Frequency for the Vessel (Empty.) is 31.8010 Hz.The Natural Frequency for the Vessel (Empty.) is 31.8010 Hz. The Natural Frequency for the Vessel (Ope...) is 16.5138 Hz. The Natural Frequency for the Vessel (Ope...) is 16.5138 Hz. The Natural Frequency for the Vessel (Filled) is 16.8513 Hz. The Natural Frequency for the Vessel (Filled) is 16.8513 Hz.
PVElite is a registered trademark of COADE, Inc. [2009]
PVElite is a registered trademark of COADE, Inc. [2009]
FileName
FileName : : Sample Sample 4.1 4.1 --- --- Page Page 21 21 of of 6262 Earthquake
Earthquake Load Load Calculation Calculation : : Step: Step: 8 8 8:15a 8:15a Apr Apr 15,201015,2010
Earthquake Analysis Results per IBC-2000 Earthquake Analysis Results per IBC-2000
User
User Entered Entered Table Table Value Value 1615.1.2(1) 1615.1.2(1) Fa Fa 1.2001.200 User
User Entered Entered Table Table Value Value 1615.1.2(1) 1615.1.2(1) Fv Fv 2.8002.800 Max.
Max. Mapped Mapped Acceleration Acceleration Value Value for for Short Short Periods Periods Ss Ss 0.750.75 Max.
Max. Mapped Mapped Acceleration Acceleration Value Value for for 1 1 sec. sec. Period Period S1 S1 0.3000.300 Moment
Moment Reduction Reduction Factor Factor Tau Tau 1.0001.000 Force
Force Modification Modification Factor Factor R R 2.0002.000 Importance
Importance Factor Factor I I 1.0001.000 Site
Site Class Class EE
Sms = Fa * Ss = 1.200 * 0.750 = 0.900 Sms = Fa * Ss = 1.200 * 0.750 = 0.900 Sm1 = Fv * S1 = 2.800 * 0.300 = 0.840 Sm1 = Fv * S1 = 2.800 * 0.300 = 0.840 Sds = 2/3 * Sms = 2/3 * 0.900 = 0.600 Sds = 2/3 * Sms = 2/3 * 0.900 = 0.600 Sd1 = 2/3 * Sm1 = 2/3 * 0.840 = 0.560 Sd1 = 2/3 * Sm1 = 2/3 * 0.840 = 0.560
Check the Period (1/Frequency) from 16-39
Check the Period (1/Frequency) from 16-39
= Ct * hn^(3/4) where Ct = 0.020 and hn = total Vessel Height [Ta]:
= Ct * hn^(3/4) where Ct = 0.020 and hn = total Vessel Height [Ta]:
= 0.020 * 161.3085 ^(3/4) = 0.140 seconds
= 0.020 * 161.3085 ^(3/4) = 0.140 seconds
The Co
The Coefficient Cu from Table
efficient Cu from Table 1617.4.2 is
1617.4.2 is 1.200
1.200
Check the Min. Value of T which is the Smaller of Cu*Ta and T, [T]:
Check the Min. Value of T which is the Smaller of Cu*Ta and T, [T]:
= Min. Value of (1.200 * 0.140 , 1/16.514 ) = 0.0606 per 1617.4.2 = Min. Value of (1.200 * 0.140 , 1/16.514 ) = 0.0606 per 1617.4.2
Compute the Seismic Response Coefficient Cs per 16-35, [Cs]:
Compute the Seismic Response Coefficient Cs per 16-35, [Cs]:
= Sds / ( R / I )= Sds / ( R / I )
= 0.600 / ( 2.00 / 1.00 ) = 0.3000 = 0.600 / ( 2.00 / 1.00 ) = 0.3000
Check the Maximum value of Cs per eqn. 16-36 :
Check the Maximum value of Cs per eqn. 16-36 :
= Sd1 / ( ( R / I )
= Sd1 / ( ( R / I ) * T )* T )
= 0.560 / ( ( 2.00 / 1.00 ) *
= 0.560 / ( ( 2.00 / 1.00 ) * 0.061 ) = 4.62390.061 ) = 4.6239
Check the Minimum value of Cs per eqn. 16-75:
Check the Minimum value of Cs per eqn. 16-75:
= 0.14 * 1.00 * 0.600 = 0.0840 = 0.14 * 1.00 * 0.600 = 0.0840For Categories E and F, check Minimum value of Cs per 16-76:
For Categories E and F, check Minimum value of Cs per 16-76:
= 0.8 * S1 / ( R / I = 0.8 * S1 / ( R / I ))
= 0.8 * 0.30 / ( 2.00 / 1.00 ) =
= 0.8 * 0.30 / ( 2.00 / 1.00 ) = 0.12000.1200
Compute the Total Base Shear V = Cs * Total Weight, [V]:
Compute the Total Base Shear V = Cs * Total Weight, [V]:
= 0.3000 * 18203.3 = 5460.98 lbf = 0.3000 * 18203.3 = 5460.98 lbf
Note: Loads multiplied by the Scalar multiplier value of 0.7143
Note: Loads multiplied by the Scalar multiplier value of 0.7143
Final
Final Base Base Shear, Shear, V V = = 3900.78 3900.78 lbflbf
Distribute the Base shear force to each element according to
Distribute the Base shear force to each element according to
the equations Fx = Cvx * V (eqn. 16-41 ) and the vertical
the equations Fx = Cvx * V (eqn. 16-41 ) and the vertical
distribution factor equation Cvx = Wx*hx**k/( Sum of Wi*hi**k ).
distribution factor equation Cvx = Wx*hx**k/( Sum of Wi*hi**k ).
The factor k in the equation is an exponent that is related to the period
The factor k in the equation is an exponent that is related to the period
of Vibration.
of Vibration. In this
In this case, the
case, the value
value of k
of k was
was 1.0000
1.0000 ..
The Natural Frequency for the Vessel (Ope...) is 16.5138 Hz. The Natural Frequency for the Vessel (Ope...) is 16.5138 Hz. Earthquake Load CalculationFileName
FileName : : Sample Sample 4.1 4.1 --- --- Page Page 22 22 of of 6262 Earthquake
Earthquake Load Load Calculation Calculation : : Step: Step: 8 8 8:15a 8:15a Apr Apr 15,201015,2010 |
| | | Earthquake Earthquake | | Earthquake Earthquake | | Element Element | | Element Element || From|
From| To To | | Height Height | | Weight Weight | | Ope Load Ope Load | | Emp Emp Load Load || | | | | in in | | lbf lbf | | lbf lbf | | lbf lbf || 10| 10| 20| 20| 0.75000 0.75000 | | 1590.89 1590.89 | | 4.13242 4.13242 | | 1.20658 1.20658 || 20|Legs| 20|Legs| 14.0004 14.0004 | | 1569.98 1569.98 | | 76.1271 76.1271 | | 9.70704 9.70704 || Legs| Legs| 30| 30| 67.7502 67.7502 | | 13501.4 13501.4 | | 3168.05 3168.05 | | 403.961 403.961 || 30| 30| 40| 40| 122.250 122.250 | | 1541.01 1541.01 | | 652.466 652.466 | | 203.585 203.585 ||
PVElite is a registered trademark of COADE, Inc. [2009]
FileName
FileName : : Sample Sample 4.1 4.1 --- --- Page Page 23 23 of of 6262 Wind/Earthquake
Wind/Earthquake Shear, Shear, Bending Bending : : Step: Step: 9 9 8:15a 8:15a Apr Apr 15,201015,2010
The following table is for the Operating Case. The following table is for the Operating Case. Wind/
Wind/ Earthquake ShearEarthquake Shear, , BendingBending
|
| | | Distance Distance to| to| Cummulative|Earthquake Cummulative|Earthquake | | Wind Wind | | Earthquake Earthquake || From|
From| To To | | Support| Support| Wind Wind Shear| Shear| Shear Shear | | Bending Bending | | Bending Bending || | |
| | in in | | lbf lbf | | lbf lbf | | in-lb in-lb | | in-lb in-lb || 10| 10| 20| 20| 17.6485 17.6485 | | 0.00000 0.00000 | | 0.00000 0.00000 | | 0.00000 0.00000 | | 0.00000 0.00000 || 20|Legs| 20|Legs| 6.25020 6.25020 | | 0.00000 0.00000 | | 4.13242 4.13242 | | 0.00000 0.00000 | | 15.0755 15.0755 || Legs| Legs| 30| 30| 53.7498 53.7498 | | 0.00000 0.00000 | | 3824.65 3824.65 | | 0.00000 0.00000 | | 242260. 242260. || 30| 30| 40| 40| 111.148 111.148 | | 0.00000 0.00000 | | 652.466 652.466 | | 0.00000 0.00000 | | 2380.27 2380.27 ||
PVElite is a registered trademark of COADE, Inc. [2009]
FileName
FileName : : Sample Sample 4.1 4.1 --- --- Page Page 24 24 of of 6262 Longitudinal
Longitudinal Stress Stress Constants Constants : : Step: Step: 10 10 8:15a 8:15a Apr Apr 15,201015,2010
Longitudinal Stress Constants Longitudinal Stress Constants
|
| | | Metal Metal Area Area | | Metal Metal Area Area |New |New & & Cold Cold | | Corroded Corroded || From|
From| To To | | New New & & Cold Cold | | Corroded Corroded |Sect. |Sect. Mod. Mod. | | Sect. Sect. Mod. Mod. || |
| | | in² in² | | in² in² | | in in ³ ³ | | in in ³ ³ || 10| 10| 20| 20| 125.803 125.803 | | 102.722 102.722 | | 1845.06 1845.06 | | 1512.84 1512.84 || 20| 20| 30| 30| 93.4624 93.4624 | | 70.2440 70.2440 | | 1378.76 1378.76 | | 1040.57 1040.57 || 30| 30| 40| 40| 125.803 125.803 | | 102.722 102.722 | | 1845.06 1845.06 | | 1512.84 1512.84 ||
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FileName
FileName : : Sample Sample 4.1 4.1 --- --- Page Page 25 25 of of 6262 Longitudinal
Longitudinal Allowable Allowable Stresses Stresses : : Step: Step: 11 11 8:15a 8:15a Apr Apr 15,201015,2010
Longitudinal Allowable Stresses Longitudinal Allowable Stresses
|
| | | All. All. Str. Str. | | All. All. Str. Str. | | All. All. Str. Str. | | All. All. Str. Str. || From| To | Long. Ten. | Hydr. Ten. |Long. Com. | Hyr. Comp. | From| To | Long. Ten. | Hydr. Ten. |Long. Com. | Hyr. Comp. |
|
| | | psi psi | | psi psi | | psi psi | | psi psi || 10| 20| 10| 20| 14000.0 14000.0 | | 18200.0 18200.0 | -15476.5 | -15476.5 | | -24091.2 -24091.2 || 20|Legs| 20|Legs| 14000.0 14000.0 | | 18200.0 18200.0 | -| -14189.7 14189.7 | | -22769.8 -22769.8 || Legs| 3 Legs| 30| 0| 14000.0 14000.0 | | 18200.0 18200.0 | -14189.7 | -14189.7 | | -22769.8 -22769.8 || 30| 40| 30| 40| 14000.0 14000.0 | | 18200.0 18200.0 | -15476.5 | -15476.5 | | -24091.2 -24091.2 ||
PVElite is a registered trademark of COADE, Inc. [2009]
FileName
FileName : : Sample Sample 4.1 4.1 --- --- Page Page 26 26 of of 6262 Longitudinal
Longitudinal Stresses Stresses Due Due to to . . . Step: Step: 12 12 8:15a 8:15a Apr Apr 15,201015,2010
Longitudinal Stress Report Longitudinal Stress Report
Note: Longitudinal Operating and Empty Stresses are computed in the
Note: Longitudinal Operating and Empty Stresses are computed in the
corroded condition. Stresses due to loads in the hydrostatic test
corroded condition. Stresses due to loads in the hydrostatic test
cases have been computed in the new and cold condition.
cases have been computed in the new and cold condition.
Longitudinal Stresses Due to . . . Longitudinal Stresses Due to . . .
|
| | | Long. Long. Str. Str. | | Long. Long. Str. Str. |Long. |Long. Str. Str. || From| To | Int. Pres. | Ext. Pres. |Hyd. Pres. | From| To | Int. Pres. | Ext. Pres. |Hyd. Pres. |
|
| | | psi psi | | psi psi | | psi psi || 10| 10| 20| 20| 3985.91 3985.91 | | 0.00000 0.00000 | | 4788.09 4788.09 || 20| 20| 30| 30| 5895.00 5895.00 | | 0.00000 0.00000 | | 6518.42 6518.42 || 30| 30| 40| 40| 3985.91 3985.91 | | 0.00000 0.00000 | | 4788.09 4788.09 ||
Longitudinal Stresses Due to . . . Longitudinal Stresses Due to . . .
|
| | | Wght. Wght. Str. Str. | | Wght. Wght. Str. Str. |Wght. |Wght. Str. Str. | | Wght. Wght. Str. Str. | | Wght. Wght. Str. Str. || From|
From| To To | | Empty Empty | | Operating Operating |Hydrotest |Hydrotest | | Emp. Emp. Mom. Mom. | | Opr. Opr. Mom. Mom. || |
| | | psi psi | | psi psi | | psi psi | | psi psi | | psi psi || 10| 10| 20| 20| 7.58650 7.58650 | | 15.4873 15.4873 | | 12.0229 12.0229 | | 0.00000 0.00000 | | 0.00000 0.00000 || 20|Legs| 20|Legs| 15.8755 15.8755 | | 44.9984 44.9984 | | 32.9812 32.9812 | | 0.18168 0.18168 | | 0.18168 0.18168 || Legs| 30| Legs| 30| -52.6021 -52.6021 | | -214.145 -214.145 | -160.934 | -160.934 | | 1.56237 1.56237 | | 1.56237 1.56237 || 30| 40| 30| 40| -7.85317 -7.85317 | | -15.0017 | -12.2407 -15.0017 | -12.2407 | | 0.00000 0.00000 | | 0.00000 0.00000 ||
Longitudinal Stresses Due to . . . Longitudinal Stresses Due to . . .
|
| | | Wght. Wght. Str. Str. | | Bend. Bend. Str. Str. |Bend. |Bend. Str. Str. | | Bend. Bend. Str. Str. | | Bend. Bend. Str. Str. || From|
From| To To | | Hyd. Hyd. Mom. Mom. | | Oper. Oper. Wind Wind |Oper. |Oper. Equ. Equ. | | Hyd. Hyd. Wind Wind | | Hyd. Hyd. Equ. Equ. || |
| | | psi psi | | psi psi | | psi psi | | psi psi | | psi psi || 10| 10| 20| 20| 0.00000 0.00000 | | 0.00000 0.00000 | | 0.00000 0.00000 | | 0.00000 0.00000 | | 0.00000 0.00000 || 20|Legs| 20|Legs| 0.13711 0.13711 | | 0.00000 0.00000 | | 0.014488 0.014488 | | 0.00000 0.00000 | | 0.00000 0.00000 || Legs| Legs| 30| 30| 1.17914 1.17914 | | 0.00000 0.00000 | | 232.814 232.814 | | 0.00000 0.00000 | | 0.00000 0.00000 || 30| 30| 40| 40| 0.00000 0.00000 | | 0.00000 0.00000 | | 1.57338 1.57338 | | 0.00000 0.00000 | | 0.00000 0.00000 ||
Longitudinal Stresses Due to . . . Longitudinal Stresses Due to . . .
|
| | | Long. Long. Str. Str. | | Long. Long. Str. Str. |Long. |Long. Str. Str. | | EarthQuake EarthQuake || From|
From| To To | | Vortex Vortex Ope.| Ope.| Vortex Vortex Emp.|Vortex Emp.|Vortex Tst.| Tst.| Empty Empty || |
| | | psi psi | | psi psi | | psi psi | | psi psi || 10| 10| 20| 20| 0.00000 0.00000 | | 0.00000 0.00000 | | 0.00000 0.00000 | | 0.00000 0.00000 || 20|Legs| 20|Legs| 0.00000 0.00000 | | 0.00000 0.00000 | | 0.00000 0.00000 | 0.00| 0.0042301 42301 || Legs| Legs| 30| 30| 0.00000 0.00000 | | 0.00000 0.00000 | | 0.00000 0.00000 | | 42.5349 42.5349 || 30| 30| 40| 40| 0.00000 0.00000 | | 0.00000 0.00000 | | 0.00000 0.00000 | | 0.49093 0.49093 ||
Longitudinal Stresses Due to . . . Longitudinal Stresses Due to . . .
|
| | | Long. Long. Str. Str. | | Long. Long. Str. Str. || From| To | Y Forces W | Y ForceS S | From| To | Y Forces W | Y ForceS S |
|
| | | psi psi | | psi psi || 10| 10| 20| 20| 0.00000 0.00000 | | 0.00000 0.00000 || 20|Legs| 20|Legs| 0.00000 0.00000 | | 0.00000 0.00000 || Legs| Legs| 30| 30| 0.00000 0.00000 | | 0.00000 0.00000 || 30| 30| 40| 40| 0.00000 0.00000 | | 0.00000 0.00000 || Long. Stress
Long. Stresses due to User Forces and Mes due to User Forces and M omentsoments
|
FileName
FileName : : Sample Sample 4.1 4.1 --- --- Page Page 27 27 of of 6262 Longitudinal
Longitudinal Stresses Stresses Due Due to to . . . Step: Step: 12 12 8:15a 8:15a Apr Apr 15,201015,2010 From|
From| To To | | Corroded Corroded | | Corroded Corroded | | No No Corr. Corr. | | No No Corr. Corr. || |
| | | psi psi | | psi psi | | psi psi | | psi psi || 10| 10| 20| 20| 0.00000 0.00000 | | 0.00000 0.00000 | | 0.00000 0.00000 | | 0.00000 0.00000 || 20|Legs| 20|Legs| 0.00000 0.00000 | | 0.00000 0.00000 | | 0.00000 0.00000 | | 0.00000 0.00000 || Legs| Legs| 30| 30| 0.00000 0.00000 | | 0.00000 0.00000 | | 0.00000 0.00000 | | 0.00000 0.00000 || 30| 30| 40| 40| 0.00000 0.00000 | | 0.00000 0.00000 | | 0.00000 0.00000 | | 0.00000 0.00000 ||