floating head exchanger design
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FLOATING HEAD EXCHANGER DESIGN CREATED BY : PR
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DEEP NAYAK FROM MUMBAI, INDIA
D I M E N S I O N S
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ISIT :
F A C T O R
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1' ('%(((-7
1' ('%(((-7
1' ('%(((-7
1' ('%(((-7
1%((
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rial Ma"i#$# Allo%a&
Grae 230 to !0 65 100 15 150 00 50
1407 1407 1407 1407 1407 1407 14071%(. 1%(. 1%(. 1%(. 1%(. 1%(. 11/%
L 1173 1173 1173 1173 1173 1111 1050
1407 1407 1407 1387 1366 1356 1285
L 1173 1173 1173 1173 1173 1122 1050
1407 1285 1152 101 1050 76 17
1%(. 1%(. 1%(. 1%(. 1%(. 1%(. 11/%
1407 1407 1407 1407 1407 1407 1387
1407 1407 1407 1407 1407 1407 1387
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le Stre''( )*+c#, -or Metal e#perat$re( /
300 35 350 35 !00 !5 !50 !5
1407 1407 1407 1407 1407 137 1366 1011(71 1(/1 1(.( 778 7(7 8/7 /.- /
76 60 46 27 08 85 883
1213 1183 1162 1142 1132 1122 1101 1101
6 77 60 47 34 15 01 <
876 858 838 821 808 788 775 763
1(71 1(/1 1(.( 778 7(7 8/7 /.- /
1315 1275 1244 113 1030 856 683 521
1315 1275 1244 113 1030 856 683 521
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BODY FLANGE 1
DESIGN DATA
Ousi4e 4i*$eer )= H*nge A 1,558
Insi4e 4i*$eer )= H*nge5#)rr)4e46 B 1,399B)le )= b)l Db 22
Cr)ss se#i)n *re* &er * b)l Ar 272.42
Ousi4e 4i*$eer )= g*s!e do 1,470
N 15
Thi#!ness )= g*s!e Tg 3
Thi#!ness )= hub * s$*ll en4 go 14
Thi#!ness )= hub * b*#! )= H*nge g1 21.0.
C)rr)si)n *ll)+*n#e CA 0
Iner$*l 4esign &ressure P 15
M*' *ll)+*ble sress * 4esign e$&r* Sfb 1173
M*' *ll)+*ble sress * *$ e$&r*u Sfa 1173Gasket : 4 f2ber 52th 62tab4e b2de
*s e )r ) n #)n *#
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1.000
d 1805288.8
F*#)r e,eF"h) e 0.006
L 1.858
Basic gasket seating i8th ;
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S!1 1027.851
S!% 528.551
S"1 60.199
S"% 30.956
ST1 (559.604)
ST% (19.367)
S is $) S### <
1.5*Sf=2636.55
SR is n) SR6 .199 <
Sf=1757.7
ST is n) ST(19.367) <
Sf=1757.7
5SSR6" 544. 25 <
Sf=1757.7
5SST6" &5 4.242 <
Sf=1757.7
1ALL CONDITIONS ARE SATISFACTOR>1
6"MIX" SED THIC7NEES OF FLANGE The re9uire4 =)r he n) )&ering #)n4i t1
81.45
The re9uire4 =)r he )&ering #)n4ii)ns t%113.58
Design hi#!ness )= H*nge ,T$Mi'Tm 113.58
ness %9 'ange is114
mm.
hickness ?se8 %912
mm. 'SU(C(NT'
0)ngiu4in*l hub sress ,S=GM)"50G
0)ngiu4in*l hub sress ,S=GMg"50G
R*4i*l H*nge sress ,SR51'..GG
R*4i*l H*nge sress ,SR51'..GG
T*ngeni*l H*nge sress ,STYGM)"5%G
T*ngeni*l H*nge sress ,STYGMg"5%G
)"CHEC7ED CODITIONS ,CNS-.-!/$"60
N,T
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BODY FLANGE
DESIGN DATA
$$ Ousi4e 4i*$eer )= H*nge A 1,558
$$ Insi4e 4i*$eer )= H*nge5#)rr)4e46 B 1,250$$ B)le )= b)l Db 22
Cr)ss se#i)n *re* &er * b)l Ar 272.42
$$ Ousi4e 4i*$eer )= g*s!e do 1,470
$$ N 15
$$ Thi#!ness )= g*s!e Tg 3
$$ Thi#!ness )= hub * s$*ll en4 go 14
$$ Thi#!ness )= hub * b*#! )= H*nge g1 21.0.
$$ C)rr)si)n *ll)+*n#e CA 0
Iner$*l 4esign &ressure P 15
M*' *ll)+*ble sress * 4esign e$&r* Sfb 1173
M*' *ll)+*ble sress * *$ e$&r*u Sfa 11738CA 1*3 Gasket : 4 f2ber 52th 62tab4e b2de
*s e )r ) n #)n *#
-
8/16/2019 Floating Head Exchanger Design
478/829
1.000
d 848691.2
1"$$ F*#)r e,eF"h) e 0.006
L 4.248
$$ Basic gasket seating i8th ;
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8/16/2019 Floating Head Exchanger Design
479/829
S!1 1184.278
S!% 258.661
S"1 56.651
S"% 12.373
ST1 (261.068)
ST% (40.253)
S is $) S### <
1.5*Sf=2636.55
SR is n) SR56.651 <
Sf=1757.7
ST is n) ST(4 .253) <
Sf=1757.7
5SSR6" 62 .464 <
Sf=1757.7
5SST6" &572. 12 <
Sf=1757.7
1ALL CONDITIONS ARE SATISFACTOR>1
6"MIX" SED THIC7NEES OF FLANGE$$ The re9uire4 =)r he n) )&ering #)n4i t1
6 .76
$$ The re9uire4 =)r he )&ering #)n4ii)ns t%13 .
$$ Design hi#!ness )= H*nge ,T$Mi'Tm 13 .
ness %9 'ange is13
mm.
hickness ?se8 %914
mm. 'SU(C(NT'
Kg"#$% 0)ngiu4in*l hub sress ,S=GM)"50G
Kg"#$% 0)ngiu4in*l hub sress ,S=GMg"50G
Kg"#$% R*4i*l H*nge sress ,SR51'..GG
Kg"#$% R*4i*l H*nge sress ,SR51'..GG
Kg"#$% T*ngeni*l H*nge sress ,STYGM)"5%G
Kg"#$% T*ngeni*l H*nge sress ,STYGMg"5%G
)"CHEC7ED CODITIONS ,CNS-.-!/$"60
Kg"#$%
Kg"#$%
Kg"#$%
Kg"#$%
Kg"#$%
N,T
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480/829
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496/829
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497/829
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498/829
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499/829
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516/829
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517/829
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518/829
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519/829
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520/829
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521/829
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526/829
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527/829
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528/829
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529/829
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530/829
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531/829
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532/829
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533/829
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534/829
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535/829
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536/829
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537/829
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538/829
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539/829
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540/829
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541/829
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542/829
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8/16/2019 Floating Head Exchanger Design
543/829
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544/829
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8/16/2019 Floating Head Exchanger Design
545/829
BODY FLANGE 3
DESIGN DATA
$$ Ousi4e 4i*$eer )= H*nge A 1,409
$$ Insi4e 4i*$eer )= H*nge5#)rr)4e46 B 1,250$$ B)le )= b)l Db 22
Cr)ss se#i)n *re* &er * b)l Ar 272.42
$$ Ousi4e 4i*$eer )= g*s!e do 1,322
$$ N 15
$$ Thi#!ness )= g*s!e Tg 3
$$ Thi#!ness )= hub * s$*ll en4 go 14
$$ Thi#!ness )= hub * b*#! )= H*nge g1 21.0.
$$ C)rr)si)n *ll)+*n#e CA 0
Iner$*l 4esign &ressure P 15
M*' *ll)+*ble sress * 4esign e$&r* Sfb 1173
M*' *ll)+*ble sress * *$ e$&r*u Sfa 11738CA 1*3 Gasket : f2ber 52th 62tab4e b2d
*s e )r ) n #)n *#
-
8/16/2019 Floating Head Exchanger Design
546/829
1.000
d 1537131.9
1"$$ F*#)r e,eF"h) e 0.006
L 1.758
$$ Basic gasket seating i8th ;
-
8/16/2019 Floating Head Exchanger Design
547/829
S!1 987.825
S!% 556.874
S"1 67.855
S"% 38.253
ST1 (567.709)
ST% 9.574
S is $) S987.825 <
1.5*Sf=2636.55
SR is n) SR67.855 <
Sf=1757.7
ST is n) ST9.574 <
Sf=1757.7
5SSR6" 527.84 <
Sf=1757.7
5SST6" &498.699 <
Sf=1757.7
1ALL CONDITIONS ARE SATISFACTOR>1
6"MIX" SED THIC7NEES OF FLANGE$$ The re9uire4 =)r he n) )&ering #)n4i t1
77.17
$$ The re9uire4 =)r he )&ering #)n4ii)ns t%1 2.79
$$ Design hi#!ness )= H*nge ,T$Mi'Tm 1 2.79
ness %9 'ange is1 3
mm.
hickness ?se8 %911
mm. 'SU(C(NT'
Kg"#$% 0)ngiu4in*l hub sress ,S=GM)"50G
Kg"#$% 0)ngiu4in*l hub sress ,S=GMg"50G
Kg"#$% R*4i*l H*nge sress ,SR51'..GG
Kg"#$% R*4i*l H*nge sress ,SR51'..GG
Kg"#$% T*ngeni*l H*nge sress ,STYGM)"5%G
Kg"#$% T*ngeni*l H*nge sress ,STYGMg"5%G
)"CHEC7ED CODITIONS ,CNS-.-!/$"60
Kg"#$%
Kg"#$%
Kg"#$%
Kg"#$%
Kg"#$%
N,T
-
8/16/2019 Floating Head Exchanger Design
548/829
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8/16/2019 Floating Head Exchanger Design
549/829
-
8/16/2019 Floating Head Exchanger Design
550/829
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8/16/2019 Floating Head Exchanger Design
551/829
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8/16/2019 Floating Head Exchanger Design
552/829
-
8/16/2019 Floating Head Exchanger Design
553/829
-
8/16/2019 Floating Head Exchanger Design
554/829
-
8/16/2019 Floating Head Exchanger Design
555/829
-
8/16/2019 Floating Head Exchanger Design
556/829
-
8/16/2019 Floating Head Exchanger Design
557/829
-
8/16/2019 Floating Head Exchanger Design
558/829
-
8/16/2019 Floating Head Exchanger Design
559/829
-
8/16/2019 Floating Head Exchanger Design
560/829
-
8/16/2019 Floating Head Exchanger Design
561/829
-
8/16/2019 Floating Head Exchanger Design
562/829
-
8/16/2019 Floating Head Exchanger Design
563/829
-
8/16/2019 Floating Head Exchanger Design
564/829
-
8/16/2019 Floating Head Exchanger Design
565/829
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8/16/2019 Floating Head Exchanger Design
566/829
-
8/16/2019 Floating Head Exchanger Design
567/829
-
8/16/2019 Floating Head Exchanger Design
568/829
-
8/16/2019 Floating Head Exchanger Design
569/829
-
8/16/2019 Floating Head Exchanger Design
570/829
-
8/16/2019 Floating Head Exchanger Design
571/829
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572/829
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8/16/2019 Floating Head Exchanger Design
573/829
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574/829
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575/829
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576/829
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577/829
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578/829
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579/829
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580/829
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581/829
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582/829
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583/829
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584/829
-
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585/829
-
8/16/2019 Floating Head Exchanger Design
586/829
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587/829
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588/829
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589/829
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8/16/2019 Floating Head Exchanger Design
590/829
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591/829
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592/829
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593/829
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594/829
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595/829
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596/829
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597/829
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598/829
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599/829
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600/829
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601/829
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602/829
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603/829
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604/829
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607/829
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608/829
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609/829
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8/16/2019 Floating Head Exchanger Design
610/829
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8/16/2019 Floating Head Exchanger Design
611/829
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8/16/2019 Floating Head Exchanger Design
612/829
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8/16/2019 Floating Head Exchanger Design
613/829
BODY FLANGE !
DESIGN DATA
$$ Ousi4e 4i*$eer )= H*nge A 1,409
$$ Insi4e 4i*$eer )= H*nge5#)rr)4e46 B 1,250$$ B)le )= b)l Db 22
Cr)ss se#i)n *re* &er * b)l Ar 272.42
$$ Ousi4e 4i*$eer )= g*s!e do 1,322
$$ N 15
$$ Thi#!ness )= g*s!e Tg 3
$$ Thi#!ness )= hub * s$*ll en4 go 14
$$ Thi#!ness )= hub * b*#! )= H*nge g1 21.0.
$$ C)rr)si)n *ll)+*n#e CA 0
Iner$*l 4esign &ressure P 15
M*' *ll)+*ble sress * 4esign e$&r* Sfb 1173
M*' *ll)+*ble sress * *$ e$&r*u Sfa 1173r 8CA 1* Gasket : #2era4 f2ber 52th 62ta
*s e )r ) n #)n *#
-
8/16/2019 Floating Head Exchanger Design
614/829
1.000
d 1537131.9
1"$$ F*#)r e,eF"h) e 0.006
L 1.758
$$ Basic gasket seating i8th ;
-
8/16/2019 Floating Head Exchanger Design
615/829
S!1 965.524
S!% 545.724
S"1 66.324
S"% 37.487
ST1 (554.892)
ST% 10.831
S is $) S965.524 <
1.5*Sf=2636.55
SR is n) SR66.324 <
Sf=1757.7
ST is n) ST1 .831 <
Sf=1757.7
5SSR6" 515.924 <
Sf=1757.7
5SST6" &488.178 <
Sf=1757.7
1ALL CONDITIONS ARE SATISFACTOR>1
6"MIX" SED THIC7NEES OF FLANGE$$ The re9uire4 =)r he n) )&ering #)n4i t1
76.4
$$ The re9uire4 =)r he )&ering #)n4ii)ns t%1 1.62
$$ Design hi#!ness )= H*nge ,T$Mi'Tm 1 1.62
ness %9 'ange is1 2
mm.
hickness ?se8 %911
mm. 'SU(C(NT'
Kg"#$% 0)ngiu4in*l hub sress ,S=GM)"50G
Kg"#$% 0)ngiu4in*l hub sress ,S=GMg"50G
Kg"#$% R*4i*l H*nge sress ,SR51'..GG
Kg"#$% R*4i*l H*nge sress ,SR51'..GG
Kg"#$% T*ngeni*l H*nge sress ,STYGM)"5%G
Kg"#$% T*ngeni*l H*nge sress ,STYGMg"5%G
)"CHEC7ED CODITIONS ,CNS-.-!/$"60
Kg"#$%
Kg"#$%
Kg"#$%
Kg"#$%
Kg"#$%
N,T
-
8/16/2019 Floating Head Exchanger Design
616/829
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8/16/2019 Floating Head Exchanger Design
617/829
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8/16/2019 Floating Head Exchanger Design
618/829
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8/16/2019 Floating Head Exchanger Design
619/829
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620/829
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621/829
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622/829
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623/829
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624/829
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625/829
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626/829
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627/829
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628/829
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629/829
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630/829
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631/829
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8/16/2019 Floating Head Exchanger Design
632/829
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8/16/2019 Floating Head Exchanger Design
633/829
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634/829
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635/829
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8/16/2019 Floating Head Exchanger Design
636/829
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637/829
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638/829
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639/829
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640/829
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641/829
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642/829
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643/829
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644/829
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645/829
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646/829
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647/829
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648/829
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649/829
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650/829
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651/829
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652/829
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653/829
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654/829
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655/829
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656/829
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657/829
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658/829
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659/829
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660/829
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661/829
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680/829
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8/16/2019 Floating Head Exchanger Design
681/829
$$
$$$$
set
$$
$$
$$
$$
$$
$$
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4e b2der 8CA 1*1 2:h
=
$$
$$%
Kg"#$%2
Kg"#$%
Kg"#$%
g #$
g #$
Kg"#$%
-
8/16/2019 Floating Head Exchanger Design
682/829
1"$$
$$$$
$$
Kg
Kg
Kg
Kg
Kg
Kg
$$$$
$$
$$
!g
-
8/16/2019 Floating Head Exchanger Design
683/829
$$
$$
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Kg"#$%
Kg"#$%
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Kg"#$%
Kg"#$%
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Kg"#$%
Kg"#$%
Kg"#$%
-
8/16/2019 Floating Head Exchanger Design
684/829
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8/16/2019 Floating Head Exchanger Design
685/829
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8/16/2019 Floating Head Exchanger Design
686/829
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