CademPVD by CADEM Softwares
Most value for money software for the mechanical design of process equipment
Trial version available on our website www.cadem.in
Pressure Vessels
Reaction Vessels
Agitator Shafts
Heat Exchangers
Process Columns
Storage Tank
Floating Roof
Chimney
•
ASME Sec. VIII Div. 1
TEMA
EEUA
IS 2825
EN 13445
API 650
API 620
IS 6533
28 years of equipment design experience captured, polished, compacted and is now ready for transfer to
designers, fabricators and plant engineers
•
Intelligent, works with minimum inputs
For instance, in case of say a body flange, the software automatically evaluates optimum configuration of
all undefined parameters: Flange OD, Flange ID, PCD, Number and Size of bolts, Gasket OD & ID, etc.
meeting the requirements of the specified equipment design code.
•
Generates final design at estimation stage, saves more than 80% of your design & estimation time
•
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•
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•
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EXAMPLE NO. PV-01
DESIGN
OF
PRESSURE VESSEL (GAS FILTER)
This example covers design of a simple pressure vessel. This pressure vessel has a top
flat cover and a bottom dished end. The top cover is of bolted type and is connected to
the shell through top body flange. The pressure vessel is provided with lugs support and
lifting lug.
NOTE:
1) Link to youtube video of this design:
/>2) As you can see in the video, the inbuilt intelligence in the software generates all
information by itself. Eg: For a body flange, the software evaluates all the undefined
parameters Flange OD, Flange ID, PCD, Number and Size of bolts, Gasket OD & ID, etc.
meeting the requirements of specified equipment design code.
3) In case of any changes to the interconnected shell geometry and / or design conditions
(pressure / temperature) including material of constructions, these dimensions
automatically regenerated by the software to meet the new requirements.
4) The software can generate cost estimation and BOM in Excel.
'CademPVD' Version 14.91 by CADEM Softwares , Pune , Website www.cadem.in
Sunay Wagle, CADEM Services,
Licensee :
Pune, India
Customer
ABC Company Ltd.
Project / Equipment
Soap Plant / Gas Filter
Designed By / Revision and Date
Index
/ R00 , 30-03-2015 23:35:19
Sr. No.
Description
1
Title page & equipment info
2
Design data
3
Material of constructions
4
Effective Pressures
5
Weight summary report
6
Test pressure calculations (shell side)
7
Wind load calculations
8
Seismic load calculations
9
Design of Cover (Front)
10
Design of Cover (Front)
11
Design of Shell Flng (Front)
12
Design of Shell Flng (Front)
13
Design of Main Shell
14
Design of Dished End (Rear)
15
Design of Lug Support
16
Design of Lug Support
17
Design of N 01
18
Design of N 01
19
Design of N 01
20
Design of N 02
21
Design of N 02
22
Design of N 02
23
Design of N 03
24
Design of N 03
25
Design of Lifting Lugs
26
Foundation load data
27
C.G. Data
Page No
'CademPVD' Version 14.91 by CADEM Softwares , Pune , Website www.cadem.in
Customer
ABC Company Ltd.
Project
Soap Plant
Location
Vapi Site
Plant
EQUIPMENT INFORMATION :
Design Code
Refrigeration Plant
Equipment Name
Gas Filter
Equipment Type
Pressure Vessel
Equipment Class
N.A.
Equipment Category
N.A.
Reference Drawing No
---
Service
Compressed Gas Services
Support Type
DESIGN & REVIEWAL :
Lug Supports
ASME VIII Div.1, 10 A11
Designed By
Design Date
30-03-2015 23:35:19
Checked By
Approved By
Revision
INSPECTION & APPROVAL :
Inspection Agency
R00
Reviewed By
EQUIPMENT DATA :
---
Front end
Flat End
Front end flanged
True
Rear end
Dished End
Rear end flanged
False
Shell ID
1250 mm
Shell OD
1270 mm
Length, Shell (W.L. to W.L) / Overall
OTHER DATA :
Fabricated weight
1650 / 2254.6 mm
Empty weight + external weights
1898.3 kgf
Estimated operating weight
1926.8 kgf
Estimated hydrotest weight
4439.8 kgf
---
1898.3 kgf
'CademPVD' Version 14.91 by CADEM Softwares , Pune , Website www.cadem.in
Sunay Wagle, CADEM Services,
Licensee :
Pune, India
Customer
ABC Company Ltd.
Project / Equipment
Soap Plant / Gas Filter
Designed By / Revision and Date
/ R00 , 30-03-2015 23:35:19
VESSEL DESIGN DATA
(1) PROCESS DETAILS :
MEDIA
DENSITY
kg/m³
Operating
Process Gas
10
Design1
Process Gas
12
Hydrotest
Water
1000
Pneumatic
Process Gas
1.2
Design2
Startup
Shutdown
Upset
(2) PR. : kgf/mm² g
INT.
Operating
0.1
0.12
EXT.
0.01055
Design1
0.12
0.12
0.01055
Design2
Startup
Shutdown
Upset
(3) TEST PR. : kgf/mm² g
Based on
Hydrotest
Input Pr
MAWP
MAP
0.156
0.156
0.169
0.132
0.143
Pneumatic
0.132
(4) TEMPERATURE : °C
MIN.
MAX.
Input
MDMT
Operating
20
-14.28
100
Design1
20
-11.75
150
21.67
-11.57
50
-11.75
50
Design2
Startup
Shutdown
Upset
Hydrotest
Pneumatic
21.67
(5) ALLOWANCES : mm
Corrosion
INT.
EXT.
3
0
Polishing
0
0
(6) RADIOGRAPHY & JOINT EFFICIENCY :
RADIOGRAPHY
JOINT
EFFICIENCY
Shell
Spot + T Joints
0.85
Head
Full
1.00
'CademPVD' Version 14.91 by CADEM Softwares , Pune , Website www.cadem.in
Sunay Wagle, CADEM Services,
Licensee :
Pune, India
Customer
ABC Company Ltd.
Project / Equipment
Soap Plant / Gas Filter
Designed By / Revision and Date
VESSEL DESIGN DATA
1. MATERIAL OF CONSTRUCTION :
/ R00 , 30-03-2015 23:35:19
Shell side
Shell
SA-516 GR. 70 Plt. [UNS:K02700]
Head
SA-516 GR. 70 Plt. [UNS:K02700]
Body flange
SA-105 Frg. [UNS:K03504]
Body flange cover
SA-516 GR. 70 Plt. [UNS:K02700]
Liner
2. NOZZLE CONNECTIONS :
Shell side
Nozzle neck <= NPS 40
SA-106 GR. B Smls. Pipe
[UNS:K03006]
Flange
SA-105 Frg. [UNS:K03504]
Cover flange
SA-105 Frg. [UNS:K03504]
Nozzle NPS > 40 & < 200
SA-106 GR. B Smls. Pipe
[UNS:K03006]
Flange
SA-105 Frg. [UNS:K03504]
Cover flange
SA-105 Frg. [UNS:K03504]
Nozzle neck >= NPS 200
SA-516 GR. 70 Plt. [UNS:K02700]
Flange
SA-516 GR. 70 Plt. [UNS:K02700]
Cover flange
SA-516 GR. 70 Plt. [UNS:K02700]
Pad flange
SA-516 GR. 70 Plt. [UNS:K02700]
Pad flange cover
SA-516 GR. 70 Plt. [UNS:K02700]
Manhole flange
SA-516 GR. 70 Plt. [UNS:K02700]
Manhole cover
SA-516 GR. 70 Plt. [UNS:K02700]
Reinforcement pad
SA-516 GR. 70 Plt. [UNS:K02700]
External bolt
SA-193 GR. B7 Bolt [UNS:G41400]
External gasket
Spiral metal wound CAF filled (S.S.)
Stiffener
SA-516 GR. 70 Plt. [UNS:K02700]
Lifting lug
IS-2062 GR. A Plt.
Support
IS-2062 GR. A Plt.
Anchor bolt
Commercial CS Bolt
3. INSULATION & CLADDING:
Mat. / Density / Thk.
Rockwool (Mineral Fibre) / 136.2 kg/m³ / 25 mm
Mat. / Thk.
Al. sheet / 1.191 mm
'CademPVD' Version 14.91 by CADEM Softwares , Pune , Website www.cadem.in
Sunay Wagle, CADEM Services,
Licensee :
Pune, India
Customer
ABC Company Ltd.
Project / Equipment
Soap Plant / Gas Filter
Designed By / Revision and Date
/ R00 , 30-03-2015 23:35:19
SUMMARY OF EFFECTIVE DESIGN PRESSURES IN kgf/mm² g VS TEMPERATURE IN °C
Sr.
Item name
Temp.
No.
Inside pr.
+ve
-ve
Liquid pr.
Effective pr.
+ve
-ve
1
Cover (Front)
150
0.12
0.01055
0
0.12
0.01055
2
Shell Flng (Front)
150
0.12
0.01055
0
0.12
0.01055
3
Main Shell
150
0.12
0.01055
0
0.12
0.01055
4
Dished End (Rear)
150
0.12
0.01055
0
0.12
0.01055
5
'CademPVD' Version 14.91 by CADEM Softwares , Pune , Website www.cadem.in
Sunay Wagle, CADEM Services,
Licensee :
Pune, India
Customer
ABC Company Ltd.
Project / Equipment
Soap Plant / Gas Filter
Designed By / Revision and Date
ITEM WISE WEIGHT SUMMARY
/ R00 , 30-03-2015 23:35:19
Sr.No.
Item name
Item size
Empty
wt
Volume
Filled wt
kgf
m³
kgf
1
Cover (Front)
Blind Flange - 1420 OD x
73.411 Thk, RF, 1363 PCD,
Tgrv = 1.588
900.5
0
900.5
2
Shell Flng (Front)
Fabricated WN - 1420 OD x
1250 ID x 1363 PCD, RF,
128.692 Thk, Trgv = 1.588,
G1 = 20, G0 = 10, hf = 30
312.3
0
312.3
3
Gasket Flng (Front)
1313.5 OD x 1250 ID, 4.763
Thk
0.1
0
0.1
4
Bolt Flng (Front)
Hex Head Bolt M24 x 243.128
Lg, 56 Nos.
48.76
0
48.76
5
Main Shell
1270 OD x 10 Thk, 1650 Lg
517.1
2.025
541.4
6
Dished End (Rear)
Elliptical D/2H = 2.0, 1270 OD
x 10 Nom / 9 Min Thk, SF =
50
181.7
0.317
185.5
7
Gusset Plate
200 Long x 190 Wide x 16
Thk, 8 Nos.
38.51
0
38.51
8
Anchor Bolt
Anchor M20 x 200 Lg, 4 Nos.
1.99
0
1.99
9
Support Pad
270 Long x 292 Wide x 10
Thk, 4 Nos.
24.97
0
24.97
10
N 01
ANSIB36.10, 150 NPS Sch.80,
156 Lg
6.697
0.00262
6.728
11
Flange [N 01]
Weld Neck, ANSI B16.5, RF,
150# for 150 NPS Sch 80 Pipe
8.08
0
8.08
12
Gasket [N 01]
166.329 OD x 146.329 ID,
4.763 Thk
0.1
0
0.1
13
Bolt [N 01]
Hex Head Bolt M20 x 86.125
Lg, 8 Nos.
1.714
0
1.714
14
Counter Flng [N 01]
Weld Neck, ANSI B16.5, RF,
150# for 150 NPS Sch 80 Pipe
8.08
0
8.08
15
Reinf [N 01]
292.659 OD x 171.275 ID x 10
Thk
3.501
0
3.501
16
N 02
ANSIB36.10, 150 NPS Sch.80,
156 Lg
6.697
0.00262
6.728
17
Flange [N 02]
Weld Neck, ANSI B16.5, RF,
150# for 150 NPS Sch 80 Pipe
8.08
0
8.08
18
Gasket [N 02]
166.329 OD x 146.329 ID,
4.763 Thk
0.1
0
0.1
19
Bolt [N 02]
Hex Head Bolt M20 x 86.125
Lg, 8 Nos.
1.714
0
1.714
20
Counter Flng [N 02]
Weld Neck, ANSI B16.5, RF,
150# for 150 NPS Sch 80 Pipe
8.08
0
8.08
21
Reinf [N 02]
292.659 OD x 171.275 ID x 10
Thk
3.501
0
3.501
22
N 03
ANSIB36.10, 50 NPS Sch.160,
150 Lg
1.682
0.00022
1.684
23
Flange [N 03]
Weld Neck, ANSI B16.5, RF,
150# for 50 NPS Sch 160 Pipe
2.428
0
2.428
24
Gasket [N 03]
62.85 OD x 42.85 ID, 4.763
Thk
0.1
0
0.1
25
Bolt [N 03]
Hex Head Bolt M16 x 67.725
Lg, 4 Nos.
0.431
0
0.431
26
Bolted Cover [N 03]
Weld Neck, ANSI B16.5, RF,
150# for 50 160 NPS Pipe
2.522
0
2.522
120 Long x 70 Wide x 12 Thk,
27
Lifting Lugs
2 Nos.
1.596
0
1.596
28
Pad (Lifting Lugs)
70 Long x 170 Wide x 8 Thk, 2
Nos.
1.507
0
1.507
29
Insulation
4084.07 W x 3754.584 L, 25
Thk
52.2
0
52.2
30
Cladding
4087.811 W x 3754.584 L,
1.191 Thk
5.058
0
5.058
31
32
33
34
35
∑
2149.7
∑
4439.8
'CademPVD' Version 14.91 by CADEM Softwares , Pune , Website www.cadem.in
Sunay Wagle, CADEM Services,
Licensee :
Pune, India
Customer
ABC Company Ltd.
Project / Equipment
Soap Plant / Gas Filter
Designed By / Revision and Date
/ R00 , 30-03-2015 23:35:19
TEST PRESSURES CALCULATION AS PER UG-99 / UG-100 : Vessel Inside
Design Temperature
T
150 °C
Operating Liquid Density
r
12 kg/m³
Hydrotest Liquid Density
rh
1000 kg/m³
Hydrotest Liquid Column
Lh
2254.6 mm
Pressure ( kgf/mm² g )
Sr.
No.
Item Name
Pi
Pl
Pc
Pe
Stress Correction ( kgf/mm² )
Peff
Sfo
Sfa
Sfa
Sfo
Pt
1
Cover (Front)
0.12
0
0
0.01055
0.12
14.06
14.06
1
0.12
2
Shell Flng (Front)
0.12
0
0
0.01055
0.12
14.06
14.06
1
0.12
3
Main Shell
0.12
0
0
0.01055
0.12
14.06
14.06
1
0.12
4
Dished End (Rear)
0.12
0
0
0.01055
0.12
14.06
14.06
1
0.12
5
Min. Pr., Pt
Legend :
Pi
=
Internal positive pressure
Pl
=
Pressure due to design liquid column
Pe
=
Internal vacuum pressure
Pc
=
External negative pressure
Peff
=
Pi + Pl + Pc
Sfo
=
Allowabe stress at design temperature
Sfa
=
Allowable stress at ambient temperature
Pt
=
MAX [ Peff + Pc, Pe ] x ( Sfa / Sfo )
Test Pressure Calculations
Pressure due to hydro liquid column, [ Plh ]
= Lh x rh x 1E-09
= 0.00225 kgf/mm² g
Hydrotest pressure, [ Ph ]
= 1.3 x Pt - Plh
= 1.3 x 0.12 - 0.00225
= 0.154 kgf/mm² g
Pneumatic test pressure, [ Pn ]
= 1.1 x Pt
= 1.1 x 0.12
= 0.132 kgf/mm² g
0.12
'CademPVD' Version 14.91 by CADEM Softwares , Pune , Website www.cadem.in
Sunay Wagle, CADEM Services,
Licensee :
Pune, India
Customer
ABC Company Ltd.
Project / Equipment
Soap Plant / Gas Filter
Designed By / Revision and Date
/ R00 , 30-03-2015 23:35:19
CALC. OF MIN. DESIGN METAL TEMPERATURE
Design Mode 1 , Corroded
Condition
CODE
Vessel Inside
ASME VIII Div.1, 10 A11
Design Pressure
Pi
0.12 kgf/mm² g
T
150 °C
Design Temperature
Sr.
No.
Item Name / Material /
Group
Stress (kgf/mm²)
Thickness (mm)
MDMT (°C)
Smt
Sdt
tn
tg
tr
Tm
Tc
MDMT
1
Cover (Front)
SA-516 GR. 70 Plt.
[UNS:K02700]
Curve : B
14.06
14.06
70.41
17.6
17.6
-11.98
40.56
-52.53
2
Shell Flng (Front)
SA-105 Frg. [UNS:K03504]
Curve : B
14.06
14.06
125.7
7
6.343
-28.89
-17.14
-11.75
3
Main Shell
SA-516 GR. 70 Plt.
[UNS:K02700]
Curve : B
14.06
14.06
7
7
6.343
-28.89
-14.73
-14.16
4
Dished End (Rear)
SA-516 GR. 70 Plt.
[UNS:K02700]
Curve : B
14.06
14.06
7
7
5.364
-28.89
-14.61
-14.28
5
Max, MDMT
Legend :
Smt
=
Stress at minimum design metal temperature.
Sdt
=
Pressure due to design liquid column
tn
=
Stress at design metal temperature.
tg
=
Nominal item thickness excluding corrosion and thinning.
tr
=
Governing metal thickness for the item.
Tg
=
Required minimum thickness of the item.
Tm
=
Minimum metal temperature for the the item.
Tc
=
MDMT Correction
MDMT
=
Final MDMT for the item = Tm - Tc.
-11.75
'CademPVD' Version 14.91 by CADEM Softwares , Pune , Website www.cadem.in
Sunay Wagle, CADEM Services,
Licensee :
Pune, India
Customer
ABC Company Ltd.
Project / Equipment
Soap Plant / Gas Filter
Designed By / Revision and Date
EXTREME FIBRE ELONGATION CALCULATION
/ R00 , 30-03-2015 23:35:19
Item Name
Sr.
No.
MOC
Rf
t
mm
mm
Eqn.
No.
e
HT
%
1
Main Shell
SA-516 GR. 70 Plt. [UNS:K02700]
625
10
1
0.8
False
2
Dished End (Rear)
SA-516 GR. 70 Plt. [UNS:K02700]
1130
10
2
0.664
False
3
4
5
Legend :
Rf
=
Mean radius after forming
Ro
=
Infinity
t
=
Nominal thickness of the plate before forming
Eqn. 1
=
50 x t / Rf x [ 1 - Rf / Ro ]
Eqn. 2
=
75 x t / Rf x [ 1 - Rf / Ro ]
'CademPVD' Version 14.91 by CADEM Softwares , Pune , Website www.cadem.in
Sunay Wagle, CADEM Services,
Licensee :
Pune, India
Customer
ABC Company Ltd.
Project / Equipment
Soap Plant / Gas Filter
Designed By / Revision and Date
/ R00 , 30-03-2015 23:35:19
WIND LOAD CALCULATION
CODE
1. DESIGN CONDITIONS ( Design Mode 1 , Corroded Condition ) :
Basic wind speed
( Section 5.2 )
Vb
Wind [IS:875, 87]
Expected life of equipment
( Section 5.3.1 )
25 Years
Probability factor (Risk coeff)
( Section 5.3.1 )
Terrain category
K1
( Section 5.3.2 )
Structure class
( Section 5.3.3 )
Force coefficient (Shape factor)
3. CALCULATION OF FORCES AND MOMENTS:
0.902
Category 2
( Section 5.3.2.2 )
Topography factor
50 m/s
Class B
K3
1.3
Cf
0.8
Equivalent diameter
De
1820 mm
Overall length of equipment
L
2254.6 mm
Height of C.G. of equipment
Hcg
1807.5 mm
K2
0.98
A
4103343.3 mm²
Vz
57.44 m/s
Pz
0.0002 kgf/mm²
Size and height factor
( Section 5.3.2 )
Effective transverse cross sectional area
= De x L
Effective wind speed
= K1 x K2 x K3 x Vb
Wind pressure
= 6E-08 x Vz
2
Longitudinal force
= Cf x A x Pz
Support elevation
F
649.9 kgf
H
372.5 mm
M
932661.5 kgf-mm
Turning moment
= F x ( Hcg - H )
'CademPVD' Version 14.91 by CADEM Softwares , Pune , Website www.cadem.in
Sunay Wagle, CADEM Services,
Licensee :
Pune, India
Customer
ABC Company Ltd.
Project / Equipment
Soap Plant / Gas Filter
Designed By / Revision and Date
/ R00 , 30-03-2015 23:35:19
SEISMIC LOAD CALCULATION
CODE
1. DESIGN CONDITIONS ( Design Mode 1 , Corroded Condition ) :
Weight of equipment
Wo
Seismic [IS:1893, 02]
Importance factor
1.5
( Table-6 , 2002 )
I
1926.8 kgf
Soil profile type
Stiff Soil Profile (SD)
Foundation type
RCC footings + Tie Beams
Damping factor
5
Seismic zone
Zone III
Seismic zone factor
( Table-2 , 2002 )
Z
0.16
Response reduction factor
( Table-7 , 2002 )
R
2.9
Sa / g
2.5, Use max value
Cf
1
Ah
0.103
Spectral accelerations coeff.
Damping correction factor
Seismic coefficient
( Fig. 2 , 2002 )
( Table-3 , 2002 )
( Clause-6.4.2 , 2002 )
= 0.5 x Z x I x Cf x ( Sa / g ) x ( 1 / R )
= 0.5 x 0.16 x 1.5 x 1 x
2.5 x ( 1 / 2.9 )
2. CALCULATION OF FORCES AND MOMENTS:
Elevation of support
H
372.5 mm
Height of C.G. of equipment
Hcg
1807.5 mm
Vb
199.3 kgf
M
286034.2 kgf-mm
Seismic base shear force
= Ah x Wo
= 0.103 x 1926.8
Seismic moment of support
= Vb x ( Hcg - H )
= 199.3 x ( 1807.5 - 372.5 )
'CademPVD' Version 14.91 by CADEM Softwares , Pune , Website www.cadem.in
Sunay Wagle, CADEM Services,
Licensee :
Pune, India
Customer
ABC Company Ltd.
Project / Equipment
Soap Plant / Gas Filter
Designed By / Revision and Date
/ R00 , 30-03-2015 23:35:19
DESIGN OF FLAT BOLTED HEAD ( INTERNAL )
Cover (Front)
CODE
1. DESIGN CONDITIONS ( Design Mode 1 , Corroded Condition ) :
Design pressure
P
ASME VIII Div.1, 10 A11
Design temperature
T
150 °C
Allowance
CA
3 mm
Groove allowance
Tg
0 mm
Joint efficiency
2. COVER DATA :
M.O.C.
E
1
Code allw. stress @ design temp.
Sfo
14.06 kgf/mm²
Radiography
0.12 kgf/mm² g
Spot + T Joints
SA-516 GR. 70 Plt. [UNS:K02700]
Code allw. stress @ atm. temp.
Sfa
14.06 kgf/mm²
Young’s modulus
Ey
19888.4 kgf/mm²
A
1420 mm
Self reinforced
False
Flange OD
Thickness provided
73.41 mm
Thickness available
3. BOLTING DATA :
M.O.C.
70.41 mm
SA-193 GR. B7 Bolt [UNS:G41400]
Code allw. stress @ design temp.
Sb
17.58 kgf/mm²
Code allw. stress @ atm. temp.
Sa
17.58 kgf/mm²
Bolt PCD
PCD
1363 mm
Bolt dia.
db
24 mm
No. of bolts
4. LINER DATA :
nb
56
M.O.C.
Liner ID
mm
Liner OD
mm
Liner thk.
5. GASKET DATA :
M.O.C.
mm
Spiral metal wound CAF filled (S.S.)
Gasket seating stress
y
7.031 kgf/mm²
Gasket factor
m
3
Inside diameter
Gi
1256 mm
Outside diameter
Go
1313.5 mm
Width of gasket
N
28.75 mm
Width of gasket
( as per Table 2-5.2 )
31.75 mm
Basic gasket seating width
( as per Table 2-5.2 )
b0
14.38 mm
Effective gasket width
( as per Table 2-5.2 )
b
9.554 mm
( see Table 2-5.2 )
G
1294.4 mm
Wp
0 mm
Dia. at load reaction
Pass partition gasket width
Pass partition gasket length
Lp
0 mm
Effective pass partition gasket width
b'
0 mm
6. BOLT LOAD CALCULATIONS AS PER APPENDIX 2-5 (b1) :
Total joint - contact surface compression load [Hp]
= 2 x ( x b x G + b' x Lp ) x m x P
= 2 x ( x 9.554 x 1294.4 + 0 x 0 ) x 3 x 0.12
= 27973 kgf
Total hydrostatic end force [H]
= 0.25 x x G 2 x P
= 0.25 x x 1294.4 2 x 0.12
= 157907.4 kgf
Minimum required bolt load for operating condition [Wm1]
= Hp + H
= 27973 + 157907.4
= 185880.4 kgf
7. BOLT LOAD CALCULATIONS AS PER APPENDIX 2-5 (b2) :
Minimum required bolt load for gasket seating [Wm2]
= ( x b x G + b' x Lp ) x y
= ( x 9.554 x 1294.4 + 0 x 0 ) x 7.031
= 273152.4 kgf
8. BOLT AREAS AS PER APPENDIX 2-5 (d) :
Total required cross-sectional area of bolts [Am]
= MAX [ Wm2 / Sa , Wm1 / Sb ] ........ For Internal '+' Pr Design
= Wm2 / Sa ..................................... For External Pr & Self Sealing Design
= 15540.6 mm²
Actual bolt area using root diameter [Ab]
= 17513.9 mm²
Flange design bolt load for the gasket seating [W]
= 0.5 x ( Am + Ab ) x Sa x 1 .................... average bolt area
= Ab x Sa x 1 ..........................................full bolt area
= 307837.2 kgf ( Full bolt area and margin factor of 1 )
9. CHECK FOR GASKET CRUSHING :
Minimum gasket width required [Nmin]
= Ab x Sb / ( 2 x x y x G )
= 17513.9 x 17.58 / ( 2 x x 7.031 x 1294.4 )
= 5.384 mm
10. DESIGN CALCULATION AS PER UG 34, BOLTING CONDITION :
Required thickness for bolting condition [t]
= G x SQRT [ 1.9 x W x 0.5 x ( PCD - G ) / ( Sfa x E x G 3 ) ]
= 1294.4 x SQRT [ 1.9 x 307837.2 x 0.5 x ( 1363 - 1294.4 ) / ( 14.06 x 1 x 1294.4 3 ) ]
= 33.2 mm
11. DESIGN CALCULATION AS PER UG 34, OPERATING CONDITION :
Self reinforced
False
Factor C is user input
False
Factor C taken from fig. UG 34 or user input
0.3
Maximum factor C value
Factor C (effective)
C
0.75
0.3
C = Min ( 2 x 0.3, 0.75 ) for self reinf.
C = 0.3 in other cases
Required thickness for operating condition [t]
= G x SQRT { [ C x P / ( Sfo x E ) ] + 1.9 x Wm1 x 0.5 x ( PCD - G ) / ( Sfo x E x G 3 ) }
= 1294.4 x SQRT { [ 0.3 x 0.12 / ( 14.06 x 1 ) ] + 1.9 x 185880.4 x 0.5 x ( 1363 - 1294.4 ) /
( 14.06 x 1 x 1294.4 3 ) }
= 70.65 mm
'CademPVD' Version 14.91 by CADEM Softwares , Pune , Website www.cadem.in
Sunay Wagle, CADEM Services,
Licensee :
Pune, India
Customer
ABC Company Ltd.
Project / Equipment
Soap Plant / Gas Filter
Designed By / Revision and Date
/ R00 , 30-03-2015 23:35:19
DESIGN OF FLAT BOLTED HEAD ( EXTERNAL )
Cover (Front)
CODE
1. DESIGN CONDITIONS ( Design Mode 1 , Corroded Condition ) :
Design pressure
P
ASME VIII Div.1, 10 A11
Design temperature
T
150 °C
Allowance
CA
3 mm
Groove allowance
Tg
0 mm
Joint efficiency
2. COVER DATA :
M.O.C.
E
1
Code allw. stress @ design temp.
Sfo
14.06 kgf/mm²
Radiography
0.01055 kgf/mm² g
Spot + T Joints
SA-516 GR. 70 Plt. [UNS:K02700]
Code allw. stress @ atm. temp.
Sfa
14.06 kgf/mm²
Young’s modulus
Ey
19888.4 kgf/mm²
A
1420 mm
Self reinforced
False
Flange OD
Thickness provided
73.41 mm
Thickness available
3. BOLTING DATA :
M.O.C.
70.41 mm
SA-193 GR. B7 Bolt [UNS:G41400]
Code allw. stress @ design temp.
Sb
17.58 kgf/mm²
Code allw. stress @ atm. temp.
Sa
17.58 kgf/mm²
Bolt PCD
PCD
1363 mm
Bolt dia.
db
24 mm
No. of bolts
4. LINER DATA :
nb
56
M.O.C.
Liner ID
mm
Liner OD
mm
Liner thk.
5. GASKET DATA :
M.O.C.
mm
Spiral metal wound CAF filled (S.S.)
Gasket seating stress
y
7.031 kgf/mm²
Gasket factor
m
3
Inside diameter
Gi
1256 mm
Outside diameter
Go
1313.5 mm
Width of gasket
N
28.75 mm
Width of gasket
( as per Table 2-5.2 )
31.75 mm
Basic gasket seating width
( as per Table 2-5.2 )
b0
14.38 mm
Effective gasket width
( as per Table 2-5.2 )
b
9.554 mm
( see Table 2-5.2 )
G
1294.4 mm
Wp
0 mm
Dia. at load reaction
Pass partition gasket width
Pass partition gasket length
Lp
0 mm
Effective pass partition gasket width
b'
0 mm
6. BOLT LOAD CALCULATIONS AS PER APPENDIX 2-5 (b1) :
Total joint - contact surface compression load [Hp]
= 2 x ( x b x G + b' x Lp ) x m x P
= 2 x ( x 9.554 x 1294.4 + 0 x 0 ) x 3 x 0.01055
= 2458.4 kgf
Total hydrostatic end force [H]
= 0.25 x x G 2 x P
= 0.25 x x 1294.4 2 x 0.01055
= 13877.8 kgf
Minimum required bolt load for operating condition [Wm1]
= Hp + H
= 2458.4 + 13877.8
= 16336.3 kgf
7. BOLT LOAD CALCULATIONS AS PER APPENDIX 2-5 (b2) :
Minimum required bolt load for gasket seating [Wm2]
= ( p x b x G + b' x Lp ) x y
= ( p x 9.554 x 1294.4 + 0 x 0 ) x 7.031
= 273152.4 kgf
8. BOLT AREAS AS PER APPENDIX 2-5 (d) :
Total required cross-sectional area of bolts [Am]
= MAX [ Wm2 / Sa , Wm1 / Sb ] ........ For Internal '+' Pr Design
= Wm2 / Sa ..................................... For External Pr & Self Sealing Design
= 15540.6 mm²
Actual bolt area using root diameter [Ab]
= 17513.9 mm²
Flange design bolt load for the gasket seating [W]
= 0.5 x ( Am + Ab ) x Sa x 1 .................... average bolt area
= Ab x Sa x 1 ..........................................full bolt area
= 307837.2 kgf ( Full bolt area and margin factor of 1 )
9. CHECK FOR GASKET CRUSHING :
Minimum gasket width required [Nmin]
= Ab x Sb / ( 2 x p x y x G )
= 17513.9 x 17.58 / ( 2 x p x 7.031 x 1294.4 )
= 5.384 mm
10. DESIGN CALCULATION AS PER UG 34, BOLTING CONDITION :
Required thickness for bolting condition [t]
= G x SQRT [ 1.9 x W x 0.5 x ( PCD - G ) / ( Sfa x E x G 3 ) ]
= 1294.4 x SQRT [ 1.9 x 307837.2 x 0.5 x ( 1363 - 1294.4 ) / ( 14.06 x 1 x 1294.4 3 ) ]
= 33.2 mm
11. DESIGN CALCULATION AS PER UG 34, OPERATING CONDITION :
Self reinforced
False
Factor C is user input
False
Factor C taken from fig. UG 34 or user input
0.3
Maximum factor C value
Factor C (effective)
C
0.75
0.3
C = Min ( 2 x 0.3, 0.75 ) for self reinf.
C = 0.3 in other cases
Required thickness for operating condition [t]
= G x SQRT { [ C x P / ( Sfo x E ) ] + 1.9 x Wm1 x 0.5 x ( PCD - G ) / ( Sfo x E x G 3 ) }
= 1294.4 x SQRT { [ 0.3 x 0.01055 / ( 14.06 x 1 ) ] + 1.9 x 16336.3 x 0.5 x ( 1363 - 1294.4 ) /
( 14.06 x 1 x 1294.4 3 ) }
= 32.29 mm
'CademPVD' Version 14.91 by CADEM Softwares , Pune , Website www.cadem.in
Sunay Wagle, CADEM Services,
Licensee :
Pune, India
Customer
ABC Company Ltd.
Project / Equipment
Soap Plant / Gas Filter
Designed By / Revision and Date
/ R00 , 30-03-2015 23:35:19
FLANGE DESIGN ( INTERNAL )
Shell Flng (Front)
CODE
1. DESIGN CONDITIONS ( Design Mode 1 , Corroded Condition ) :
Design pressure
P
ASME VIII Div.1, 10 A11
Design temperature
T
150 °C
Allowance
CA
3 mm
Groove allowance
2. FLANGE DATA :
M.O.C.
Tg
0 mm
Code allw. stress @ design temp.
Sfo
14.06 kgf/mm²
0.12 kgf/mm² g
SA-105 Frg. [UNS:K03504]
Code allw. stress @ atm. temp.
Sfa
14.06 kgf/mm²
Inside diameter
B
1256 mm
Outside diameter
A
1420 mm
Hub length
h
30 mm
Thickness ( hub end )
g1
17 mm
Thickness ( pipe end )
g0
7 mm
Thickness provided
128.7 mm
Thickness available
3. BOLTING DATA :
M.O.C.
125.7 mm
SA-193 GR. B7 Bolt [UNS:G41400]
Code allw. stress @ design temp.
Sb
17.58 kgf/mm²
Code allw. stress @ atm. temp.
Sa
17.58 kgf/mm²
Bolt PCD
C
1363 mm
Bolt dia.
db
24 mm
No. of bolts
4. LINER DATA :
nb
56
M.O.C.
Liner ID
mm
Liner OD
mm
Liner thk.
5. GASKET DATA :
5a. Flange gasket data :
M.O.C.
mm
Gasket type
Ring Gasket
Gasket confinement type
Unconfined
Flange face type
Raised Face
Flange gakset surface finish
Serrated (Normal)
Counter flange face type
Raised Face
Counter gakset surface finish
Serrated (Normal)
Applicalbe gasket sketch in Table 2-5.2
Type 1B
Spiral metal wound CAF filled (S.S.)
Applicable gasket column in Table 2-5.2
Gasket seating stress
Gasket factor
( refer to Note 1, Table 2-5.1 )
( from Table 2-5.1 )
Inside diame
5b. Partition groove gasket data (For H.E. body flange) :
1
y
7.031 kgf/mm²
m
3
Gasket seating stress
( refer to Note 1, Table 2-5.1 )
Gasket factor
( from Table 2-5.1 )
y'
0 kgf/mm²
m'
0
Pass partition gasket width
Wp
0 mm
Pass partition gasket length
Lp
0 mm
Effective pass partition gasket width
b'
0 mm
6. BOLT LOAD CALCULATIONS AS PER APPENDIX 2-5 (b1)
Total joint - contact surface compression load [Hp]
= 2 x ( p x b x G x m + b' x Lp x m' ) x P
= 2 x ( p x 9.554 x 1294.4 x 3 + 0 x 0 x 0 ) x 0.12
= 27973 kgf
Total hydrostatic end force [H]
= 0.25 x p x G ² x P
= 0.25 x p x 1294.4 ² x 0.12
= 157907.4 kgf
Minimum required bolt load for operating condition [Wm1a]
= Hp + H
= 27973 + 157907.4
= 185880.4 kgf
Minimum required bolt load for operating condition [Wm1b]
( from mating flange )
= 185880.4 kgf
Governing bolt load for operating condition [Wm1]
= MAX [ Wm1a , Wm1b ]
= MAX [ 185880.4 , 185880.4 ]
= 185880.4 kgf
7. BOLT LOAD CALCULATION AS PER APPENDIX 2-5 (b2)
Minimum required bolt load for gasket seating [Wm2]
= ( p x b x G x y + b' x Lp x y' )
= ( p x 9.554 x 1294.4 x 7.031 + 0 x 0 x 0 )
= 273152.4 kgf
8. BOLT AREAS AS PER APPENDIX 2-5 (d)
Total required cross-sectional area of bolts [Am]
= MAX [ Wm2 / Sa , Wm1 / Sb ] ........ For Internal '+' Pr Design
= Wm2 / Sa ..................................... For External Pr & Self Sealing Design
= 15540.6 mm²
Actual bolt area using root diameter [Ab]
= 17513.9 mm²
Flange design bolt load for the gasket seating [W]
= 0.5 x ( Am + Ab ) x Sa x 1 .................... average bolt area
= Ab x Sa x 1 ..........................................full bolt area
= 307837.2 kgf ( Full bolt area and margin factor of 1 )
9. CHECK FOR GASKET CRUSHING
Minimum gasket width required [Nmin]
= Ab x Sb / ( 2 x p x y x G )
= 17513.9 x 17.58 / ( 2 x p x 7.031 x 1294.4 )
= 5.384 mm
10. BOLT SPACING CORRECTION FACTOR
As per Brownell & Young or IS 2825,
= SQRT [ Bolt spacing / ( 2 x db + t ) ]
As per TEMA or BS 5500,
= SQRT [ Bolt spacing / Bmax ] ................... where,
Bmax = maximum recommended bolt spacing = 2 x db + 6 x t / ( m + 0.5 )
Brownell & Young, Cf = 1 ( min. equal to 1 )
INTEGRAL FLANGE DESIGN
Shell Flng (Front)
11. LOADS AND FORCES DURING OPERATING CONDITION AS PER APPENDIX 2-3
Hydrostatic end force on area inside of flange [HD]
= 0.25 x p x B 2 x P
= 0.25 x p x 1256 2 x 0.12
= 148679.3 kgf
Gasket load (difference between flange design bolt load and total hydrostatic end force) [HG]
= Wm1 - H
= 185880.4 - 157907.4
= 27973 kgf
Difference between total hydrostatic end force and hydrostatic end force on area inside of flange [HT]
= H - HD
= 157907.4 - 148679.3
= 9228.2 kgf
12. MOMENT ARMS FOR FLANGE LOADS AS PER TABLE 2-6
Radial distance from the bolt circle to intersection of hub and back of flange, as per Appendix 2-3 [R]
= 0.5 x ( C - B ) - g1
= 0.5 x ( 1363 - 1256 ) - 17
= 36.5 mm
Radial distance from the bolt circle to the circle on which HD acts [hD]
= R + 0.5 x g1
= 36.5 + 0.5 x 17
= 45 mm
Radial distance from gasket load reaction to the bolt circle [hG]
= 0.5 x ( C - G )
= 0.5 x ( 1363 - 1294.4 )
= 34.3 mm
Radial distance from the bolt circle to the circle on which HT acts [hT]
= 0.5 x ( R + g1 + hG )
= 0.5 x ( 36.5 + 17 + 34.3 )
= 43.9 mm
13. FLANGE MOMENTS UNDER OPERATING CONDITION AS PER APPENDIX 2-6
Component of moment due to HD [MD]
= HD x hD
= 148679.3 x 45
= 6690566.9 kgf-mm
Component of moment due to HG [MG]
= HG x hG
= 27973 x 34.3
= 959588.9 kgf-mm
Component of moment due to HT [MT]
= HT x hT
= 9228.2 x 43.9
= 405136.1 kgf-mm
Total moment acting on the flange for operating condition [MO]
= MD + MG + MT
= 6690566.9 + 959588.9 + 405136.1
= 8055291.9 kgf-mm
14. LOADS AND FORCES DURING GASKET SEATING AS PER APPENDIX 2-3
Gasket load for seating condition [HG]
=W
= 307837.2 kgf
15. MOMENT UNDER GASKET SEATING AS PER APPENDIX 2-6
Total moment acting on the flange for gasket seating [MO']
= W x hG
= 307837.2 x 34.3
= 10560086 kgf-mm
16. SHAPE CONSTANTS
A/B
K
1.131
Flange factors from Fig. 2-7.1
T
1.866
Z
8.189
Y
15.84
U
17.41
e
0.00922
h0
93.77
F / h0
Factor from Fig. 2-7.2
F
0.864
Factor from Fig. 2-7.3
V
0.261
g1 / g0
2.429
h / h0
( U / V ) x h0 x g0
0.32
2
Factor from Fig. 2-7.6
17. STRESS FORMULA FACTORS
Assumed thickness [t]
= 108.7 mm
Factor [a]
=txe+1
= 108.7 x 0.00922 + 1
= 2.002
Factor [b]
= 1.333 x t x e + 1
= 1.333 x 108.7 x 0.00922 + 1
= 2.336
Factor [g]
=a/T
= 2.002 / 1.866
= 1.073
Factor [d]
=t3/d
d
306079.1
f
2.935
= 108.7 3 / 306079.1
= 4.195
Factor [l]
=g+d
= 1.073 + 4.195
= 5.268
18. FLANGE STRESSES AS PER APPENDIX 2-7 & 2-8
Equivalent moment [Mmax]
= MAX [ MO , MO' x Sfo / Sfa ]
= MAX [ 8055291.9 , 10560086 x 14.06 / 14.06 ]
= 10560086 kgf-mm
Corrected equivalent moment per unit length [M]
= Mmax x ( Cf / B )
= 10560086 x ( 1 / 1256 )
= 8407.7 kgf
Longitudinal hub stress [SH]
= f x M / ( l x g1 2 )
= 2.935 x 8407.7 / ( 5.268 x 17 2 )
= 16.21 kgf/mm²
.................................... < 1.5 x Sfo
Radial flange stress [SR]
=bxM/(lxt2)
= 2.336 x 8407.7 / ( 5.268 x 108.7 2 )
= 0.316 kgf/mm²
.................................... < Sfo
Tangential flange stress [ST]
= ( M x Y / t 2 ) - Z x SR
= ( 8407.7 x 15.84 / 108.7 2 ) - 8.189 x 0.316
= 8.69 kgf/mm²
.................................... < Sfo
Average stress
= MAX [ 0.5 x ( SH + SR ) , 0.5 x ( SH + ST ) ]
= MAX [ 0.5 x ( 16.21 + 0.316 ) , 0.5 x ( 16.21 + 8.69 ) ]
= 12.45 kgf/mm²
.................................... < Sfo
19. FLANGE RIGIDITY CHECKING AS PER APPENDIX 2-14
Modulus of elasticity for flange
Efo
19888.4 kgf/mm²
Rigidity factor
Rigidity index [J]
= 52.14 x V x Mmax / ( l x Efo x g0 2 x KI x h0 )
= 52.14 x 0.261 x 10560086 / ( 5.268 x 19888.4 x 7
= 0.996
Since J < 1.0, design is safe
KI
0.3
2
x 0.3 x 93.77 )
'CademPVD' Version 14.91 by CADEM Softwares , Pune , Website www.cadem.in
Sunay Wagle, CADEM Services,
Licensee :
Pune, India
Customer
ABC Company Ltd.
Project / Equipment
Soap Plant / Gas Filter
Designed By / Revision and Date
/ R00 , 30-03-2015 23:35:19
FLANGE DESIGN ( EXTERNAL )
Shell Flng (Front)
CODE
1. DESIGN CONDITIONS ( Design Mode 1 , Corroded Condition ) :
Design pressure
P
ASME VIII Div.1, 10 A11
Design temperature
T
150 °C
Allowance
CA
3 mm
Groove allowance
2. FLANGE DATA :
M.O.C.
Tg
0 mm
Code allw. stress @ design temp.
Sfo
14.06 kgf/mm²
0.01055 kgf/mm² g
SA-105 Frg. [UNS:K03504]
Code allw. stress @ atm. temp.
Sfa
14.06 kgf/mm²
Inside diameter
B
1256 mm
Outside diameter
A
1420 mm
Hub length
h
30 mm
Thickness ( hub end )
g1
17 mm
Thickness ( pipe end )
g0
7 mm
Thickness provided
128.7 mm
Thickness available
3. BOLTING DATA :
M.O.C.
125.7 mm
SA-193 GR. B7 Bolt [UNS:G41400]
Code allw. stress @ design temp.
Sb
17.58 kgf/mm²
Code allw. stress @ atm. temp.
Sa
17.58 kgf/mm²
Bolt PCD
C
1363 mm
Bolt dia.
db
24 mm
No. of bolts
4. LINER DATA :
nb
56
M.O.C.
Liner ID
mm
Liner OD
mm
Liner thk.
5. GASKET DATA :
5a. Flange gasket data :
M.O.C.
mm
Gasket type
Ring Gasket
Gasket confinement type
Unconfined
Flange face type
Raised Face
Flange gakset surface finish
Serrated (Normal)
Counter flange face type
Raised Face
Counter gakset surface finish
Serrated (Normal)
Applicalbe gasket sketch in Table 2-5.2
Type 1B
Spiral metal wound CAF filled (S.S.)
Applicable gasket column in Table 2-5.2
Gasket seating stress
( refer to Note 1, Table 2-5.1 )
Gasket factor
( from Table 2-5.1 )
Inside diameter
Outside diameter
1
y
7.031 kgf/mm²
m
3
Gi
1256 mm
Go
1313.5 mm
Width of gasket
( as per Table 2-5.2 )
N
28.75 mm
Width of gasket
( as per Table 2-5.2 )
w
28.75 mm
Width of raised face or gasket contact width
31.75 mm
( as per Table 2-5.2 )
Basic gasket seating width
( as per Table 2-5.2 )
b0
14.38 mm
Effective gasket width
( as per Table 2-5.2 )
b
9.554 mm
G
1294.4 mm
Dia. at load reaction
( see Table 2-5.2 )
5b. Partition groove gasket data (For H.E. body flange) :
M.O.C.
--
Gasket seating stress
( refer to Note 1, Table 2-5.1 )
Gasket factor
( from Table 2-5.1 )
y'
0 kgf/mm²
m'
0
Pass partition gasket width
Wp
0 mm
Pass partition gasket length
Lp
0 mm
Effective pass partition gasket width
b'
0 mm
6. BOLT LOAD CALCULATIONS AS PER APPENDIX 2-5 (b1)
Total joint - contact surface compression load [Hp]
= 2 x ( p x b x G x m + b' x Lp x m' ) x P
= 2 x ( p x 9.554 x 1294.4 x 3 + 0 x 0 x 0 ) x 0.01055
= 2458.4 kgf
Total hydrostatic end force [H]
= 0.25 x p x G ² x P
= 0.25 x p x 1294.4 ² x 0.01055
= 13877.8 kgf
Minimum required bolt load for operating condition [Wm1a]
= Hp + H
= 2458.4 + 13877.8
= 16336.3 kgf
Minimum required bolt load for operating condition [Wm1b]
( from mating flange )
= 16336.3 kgf
Governing bolt load for operating condition [Wm1]
= MAX [ Wm1a , Wm1b ]
= MAX [ 16336.3 , 16336.3 ]
= 16336.3 kgf
7. BOLT LOAD CALCULATION AS PER APPENDIX 2-5 (b2)
Minimum required bolt load for gasket seating [Wm2]
= ( p x b x G x y + b' x Lp x y' )
= ( p x 9.554 x 1294.4 x 7.031 + 0 x 0 x 0 )
= 273152.4 kgf
8. BOLT AREAS AS PER APPENDIX 2-5 (d)
Total required cross-sectional area of bolts [Am]
= MAX [ Wm2 / Sa , Wm1 / Sb ] ........ For Internal '+' Pr Design
= Wm2 / Sa ..................................... For External Pr & Self Sealing Design
= 15540.6 mm²
Actual bolt area using root diameter [Ab]
= 17513.9 mm²
Flange design bolt load for the gasket seating [W]
= 0.5 x ( Am + Ab ) x Sa x 1 .................... average bolt area
= Ab x Sa x 1 ..........................................full bolt area
= 307837.2 kgf ( Full bolt area and margin factor of 1 )
9. CHECK FOR GASKET CRUSHING
Minimum gasket width required [Nmin]
= Ab x Sb / ( 2 x p x y x G )
= 17513.9 x 17.58 / ( 2 x p x 7.031 x 1294.4 )
= 5.384 mm
10. BOLT SPACING CORRECTION FACTOR
As per Brownell & Young or IS 2825,
= SQRT [ Bolt spacing / ( 2 x db + t ) ]
As per TEMA or BS 5500,
= SQRT [ Bolt spacing / Bmax ] ................... where,
Bmax = maximum recommended bolt spacing = 2 x db + 6 x t / ( m + 0.5 )
Brownell & Young, Cf = 1 ( min. equal to 1 )
INTEGRAL FLANGE DESIGN
Shell Flng (Front)
11. LOADS AND FORCES DURING OPERATING CONDITION AS PER APPENDIX 2-3
Hydrostatic end force on area inside of flange [HD]
= 0.25 x p x B 2 x P
= 0.25 x p x 1256 2 x 0.01055
= 13066.8 kgf
Difference between total hydrostatic end force and hydrostatic end force on area inside of flange [HT]
= H - HD
= 13877.8 - 13066.8
= 811 kgf
12. MOMENT ARMS FOR FLANGE LOADS AS PER APPENDIX TABLE 2-6
Radial distance from the bolt circle to intersection of hub and back of flange, as per Appendix 2-3 [R]
= 0.5 x ( C - B ) - g1
= 0.5 x ( 1363 - 1256 ) - 17
= 36.5 mm
Radial distance from the bolt circle to the circle on which HD acts [hD]
= R + 0.5 x g1
= 36.5 + 0.5 x 17
= 45 mm
Radial distance from gasket load reaction to the bolt circle [hG]
= 0.5 x ( C - G )
= 0.5 x ( 1363 - 1294.4 )
= 34.3 mm
Radial distance from the bolt circle to the circle on which HT acts [hT]
= 0.5 x ( R + g1 + hG )
= 0.5 x ( 36.5 + 17 + 34.3 )
= 43.9 mm
13. FLANGE MOMENTS UNDER OPERATING CONDITION AS PER APPENDIX 2-6
Component of moment due to HD [MD]
= HD x ( hD - hG )
= 13066.8 x ( 45 - 34.3 )
= 139760.9 kgf-mm
Component of moment due to HT [MT]
= HT x ( hT - hG )
= 811 x ( 43.9 - 34.3 )
= 7784.2 kgf-mm
Total moment acting on the flange for operating condition [MO]
= MD + MT
= 139760.9 + 7784.2
= 147545.1 kgf-mm
14. LOADS AND FORCES DURING GASKET SEATING AS PER APPENDIX 2-3
Gasket load for seating condition [HG]
=W
= 307837.2 kgf
15. MOMENT UNDER GASKET SEATING AS PER APPENDIX 2-6
Total moment acting on the flange for gasket seating [MO']
= W x hG
= 307837.2 x 34.3
= 10560086 kgf-mm
16. SHAPE CONSTANTS
A/B
K
1.131
Flange factors from Fig. 2-7.1
T
1.866
Z
8.189
Y
15.84
U
17.41
h0
93.77
F / h0
e
0.00922
Factor from Fig. 2-7.2
F
0.864
Factor from Fig. 2-7.3
V
0.261
g1 / g0
2.429
h / h0
0.32
( U / V ) x h0 x g0 2
d
306079.1
Factor from Fig. 2-7.6
17. STRESS FORMULA FACTORS
Assumed thickness [t]
= 108.9 mm
Factor [a]
=txe+1
= 108.9 x 0.00922 + 1
= 2.004
Factor [b]
= 1.333 x t x e + 1
= 1.333 x 108.9 x 0.00922 + 1
= 2.338
Factor [g]
=a/T
= 2.004 / 1.866
= 1.074
Factor [d]
=t3/d
= 108.9 3 / 306079.1
= 4.217
Factor [l]
=g+d
= 1.074 + 4.217
= 5.29
18. FLANGE STRESSES AS PER APPENDIX 2-7 & 2-8
Equivalent moment [Mmax]
f
2.935