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Super Calculations

The document contains calculations for minimum required thicknesses (TMIN) of pressure vessels, piping, and pipelines based on design pressure and stress values. It includes formulas and examples for calculating TMIN and maximum pressure for cylindrical shells, heads, straight pipes, and pipelines using standards like ASME and ANSI B31.3. Joint efficiencies are provided for different head types. Maximum stresses are listed for various steel grades.

Uploaded by

Carlos Tijerina
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© © All Rights Reserved
We take content rights seriously. If you suspect this is your content, claim it here.
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Download as XLS, PDF, TXT or read online on Scribd
0% found this document useful (1 vote)
118 views12 pages

Super Calculations

The document contains calculations for minimum required thicknesses (TMIN) of pressure vessels, piping, and pipelines based on design pressure and stress values. It includes formulas and examples for calculating TMIN and maximum pressure for cylindrical shells, heads, straight pipes, and pipelines using standards like ASME and ANSI B31.3. Joint efficiencies are provided for different head types. Maximum stresses are listed for various steel grades.

Uploaded by

Carlos Tijerina
Copyright
© © All Rights Reserved
We take content rights seriously. If you suspect this is your content, claim it here.
Available Formats
Download as XLS, PDF, TXT or read online on Scribd
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TMIN CALCS
CALCULATE CORR RATE & TMIN DATE

CALCULATE TMIN DATE


(or THICKNESS at a TMIN DATE)

Calculated by:
Perry D. Koch
2 Thickness Meas's when Corr Rate is Unknown
ENTERED DATA

DATE
Meas

Earliest
02/01/95
0.460

Latest
07/22/99
0.200

CALCULATED DATA

Tmin
0.100

ENTERED DATA

DATE
Meas
Meas
Meas
Meas
Meas
Meas
Meas
Meas

Earliest
02/01/87
0.460
0.450

Latest
03/01/94
0.240
0.210

Date Revised: 09/09/2015 00:30:28

Calculated by:
Perry D. Koch
One Thickness Meas. & a Known Corr Rate

Corr
Rate
58.1

Yrs to
Tmin
1.7

TMIN
DATE
04/09/01

CALCULATED DATA

Tmin
0.100

Corr
Rate
31.1
33.9
0.0
0.0
0.0
0.0
0.0
0.0

Yrs to
TMIN
Tmin
DATE
4.5
09/01/98
6.2
05/09/00
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ENTERED DATA

Date of
Meas
06/18/97

Last
Meas

0.380

Tmin
0.120

Corr
Rate
30.9

CALC'D DATA
Yrs to
Tmin
8.4
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PDK

TMIN CALCS

CALCULATE PRESSURE VESSEL TMIN or DESIGN PRESSURE


PRESSURE VESSEL TMIN CALCS (Cylindrical shells INSIDE RADIUS) - enter DATA IN BOXES FOR CALC'N
t= PR/SE-0.6P
Minimum Required Thickness, inches
P= SEt/R+0.6t Design Pressure, psi
P=
10
Design Pressure, psi
t=
3.120
minimum required thickness
R=
457.2
INSIDE Radius of shell, inches
R=
29.0
INSIDE Radius of shell, inches
S=
1055
Maximum Allowable Stress, psi
S=
17500
Maximum Allowable Stress, psi
E=
1.00
Joint Efficiency
E=
1.00
Joint Efficiency

t=

4.360

inches,

per ASME Sect 8 UG-27(c)1

P=

1883

psi,

per ASME Sect 8 UG-27(c)1

PRESSURE VESSEL TMIN CALCS (Cylindrical shells OUTSIDE RADIUS) - enter DATA IN BOXES FOR CALC'N
t= PR/SE+0.4P
Minimum Required Thickness, inches
P= SEt/R-0.4t Design Pressure, psi
P=
40
Design Pressure, psi
t=
0.128
minimum required thickness
R=
175.6
OUTSIDE Radius of shell, inches
R=
12.0
OUTSIDE Radius of shell, inches
S=
20000
Maximum Allowable Stress, psi
S=
16600
Maximum Allowable Stress, psi
E=
1.00
Joint Efficiency
E=
0.85
Joint Efficiency

t=

0.351

FORMED ELLIPSODIAL
t= PD/2SE-0.2P
P=
10
D=
914.400
S=
1230.372
*E=
1.00

t=

3.719

inches,

ASME Sect 8 UG-27 APP 1-1

P=

150

psi

ASME Sect 8 UG-27 APP 1-1

HEADS, PRESSURE ON CONCAVE SIDE (INSIDE RADIUS) - enter DATA IN BOXES FOR CALC'N
Minimum Required Thickness, inches
P= 2SEt/D+0.2t Design Pressure, psi
Design Pressure, psi
t=
3.115
minimum required thickness
INSIDE Diametr head skirt, inches
D=
60.0
INSIDE Diametr head skirt, inches
Maximum Allowable Stress, psi
S=
16600
Maximum Allowable Stress, psi
Joint Efficiency (see table below for eff)
*E=
0.85
Joint Efficiency (see table below for eff)
inches,

per ASME Sect 8 UG-32(d)

Date Revised: 09/09/2015 00:30:29

P=

Page 4 of 12

1450

psi,

per ASME Sect 8 UG-32(d)

PDK

TMIN CALCS
FORMED ELLIPSODIAL
t= PD/2SE+1.8P
P=
3300
D=
18.0
S=
17600
*E=
0.85

t=

1.656

HEADS, PRESSURE ON CONVCAVE SIDE (OUTSIDE RADIUS) - enter DATA IN BOXES FOR CALC'N
Minimum Required Thickness, inches
P= 2SEt/D-1.8t Design Pressure, psi
Design Pressure, psi
t=
1.656
minimum required thickness
OUTSIDE Diametr head skirt, inches
D=
30.0
OUTSIDE Diametr head skirt, inches
Maximum Allowable Stress, psi
S=
17600
Maximum Allowable Stress, psi
Joint Efficiency (see table below for eff)
*E=
0.85
Joint Efficiency (see table below for eff)
inches,

P=

per ASME Sect 8 UG-32(d)

* EFFICIENCY (E) TO BE USED IN CALCULATIONS OF


SEAMLESS HEADS
TYPE OF
TYPE OF DEGREE OF EXAMINATION
HEAD
JOINT
OF HEAD TO SHELL JOINT
FULL
SPOT
NONE
Hemi-shpr
#1
1.00
0.85
0.80
Hemi-shpr
#2
0.90
0.80
0.80
All others
ANY
1.00
0.85
0.80
Excerpted from PRESSURE VESSEL HANDBOOK

Date Revised: 09/09/2015 00:30:29

Page 5 of 12

1834

psi,

per ASME Sect 8 UG-32(d)

STRESS VALUES of MATERIALS


1000 psi
SPEC
TEMP
NO.
GRADE
-20 to 650
SA-285
C
13.8
SA-515
60
15.0
SA-515
70
17.5
SA-516
60
15.0
SA-516
70
17.5

PDK

TMIN CALCS
CALCULATE PIPING TMIN
Chemical Plant & Petroleum Refinery Piping, ANSI B31.3
Straight Pipe Under Internal Pressure, 304.1.2 - enter DATA IN BOXES FOR CALC'N
t= PD/2(SE+PY) Pressure Design Thickness, inches
P=
150
Internal Design Gage Pressure
D=
6.625
Outside Diameter of Pipe, inches
SE=
15000
Allowable Stress, excluding quality or joint factors (E=1 if seamless pipe)
Y=
0.40
Coefficient from Table 304.1.1, Y=0.4 for all Ferritic Steels up to 900 F

t=

0.033

inches,

per ANSI B31.3, Para. 304.1.2

CALCULATE PIPING MAXIMUM PRESSURE


Chemical Plant & Petroleum Refinery Piping, ANSI B31.3
Straight Pipe Under Internal Pressure, 304.1.2 - enter DATA IN BOXES FOR CALC'N
P= 2SEt/(D-2tY) Internal Design Pressure, psig
t=
0.155
Pressure Design Thickness, inches
Thickness is UT 0.20 - 0.02 corrosion allowance
D=
1.05
Outside Diameter of Pipe, inches
SE=
18800
Allowable Stress, excluding quality or joint factors (E=1 if seamless pipe)
Y=
0.40
Coefficient from Table 304.1.1, Y=0.4 for all Ferritic Steels up to 900 F

P=

6294

psig,

a Kg/cm2=

442.49

per ANSI B31.3, Para. 304.1.2

CALCULATE PIPING MAXIMUM PRESSURE


Gas Transmission and Distribution Piping Systems, ANSI B31.8
Date Revised: 09/09/2015 00:30:29

Page 6 of 12

PDK

TMIN CALCS
P= (2St/D)xFxEx Internal Design Pressure, psig
S=
35000
Specified minimum yield strength
D=
16.00
Nominal outside diameter, inches
t=
0.18
Nominal wall thickness, inches
F=
0.60
Construction type design factor from Table 841.111, Construction Type B factor = 0.60, TYPE C = 0.50
E=
1.00
Lonlgitudinal joint factor from Table 841.112, 1.00 for seamless pipe
T=
1.00
Temperature derating factor from Table 841.113, for 250F or less T=1.00
P=

473

psig

CALCULATE PIPELINE INTERNAL DESIGN PRESSURE

49 CFR, Part 195, para 195.106


Straight Pipe Under Internal Pressure, 304.1.2 - enter DATA IN BOXES FOR CALC'N
P= (2St/D)xExF Internal design pressure in psig
S=
13800
YIELD strength in psi
t=
2.580
Nominal wall thickness of the pipe in inches
D=
16.0
Nominal outside diameter of the pipe in inches
E=
1.00
Seam joint factor, E=1 for all seamless pipe
F=
0.72
Design factor, F= 0.72, except for off-shore platforms

P=

3204.4

psig

Date Revised: 09/09/2015 00:30:29

Page 7 of 12

PDK

TMIN CALCS

orr Rate
CALC'D DATA

TMIN
DATE
11/14/05
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Date Revised: 09/09/2015 00:30:29

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PDK

TMIN CALCS

Date Revised: 09/09/2015 00:30:29

Page 9 of 12

PDK

TMIN CALCS

Date Revised: 09/09/2015 00:30:29

Page 10 of 12

PDK

TMIN CALCS

Date Revised: 09/09/2015 00:30:29

Page 11 of 12

PDK

TMIN CALCS

Date Revised: 09/09/2015 00:30:29

Page 12 of 12

PDK

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