106736744 Safety Valve Calc
Transcript of 106736744 Safety Valve Calc
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Safety valve nozzle M/S.CETHAR VESSELS (P ) LTDM/S.BINANI CEMENTS
SAFETY VALVE NOZZLE DESIGN CALCULATION AS PER ASME B31.1-2010
Description I!"# Unit
Safety valve set pressure = P 289.30
Design temperature !".00 °C
Nozzle material specication SA"82 #"2$%2 -
Young's Modulus of material @ design temp = E 2.8&'0! psi llo!a"le stress for saf#valve nozz#matl @ design te "8200.00 psi
$eig%t of valve = $ 22.00 kgs
Nozzle %eig%t from od of run pipe = & "(.9 mm
Dist# "et!# od of run pipe to centre line outlet pipe 8.9 mm
(un pipe outside diameter =)#D 2!3.00 mm
*%ic+ness of run pipe = *r 33.90 mm
Saf# valve nozz#od @ pipe conn ,point-./ = dn.#=r 20.00 mm
Saf# valve nozz#t%+ @pipe conn ,point-./ = *'"# 63."( mm
Saf# valve nozz#od @ valve conn ,point-/ = dn# 20.00 mm
Saf# valve nozz#t%+ @ valve conn ,point-/ = tn# 62.9 mm
0alve rise time = to 0.0 sec
Moment arm = 1 6"0.00 mm
Moment arm for point ,./ =1. "9 inch
Moment arm for point ,/ =1 "3 inch
Seismic coe2cient ".( -
verage od of saf#valve nozzle = do 8.03" inch
verage id of saf#valve nozzle = di 3.06 inch
Moment of inertia of saf#valve nozzle = 3 "99.9(
0.006669 sec
(atio = to4 * 6.00 -
Dynamic load factor ,g 33#5# of ap6#-33 of asme "5. "."" -
BENDING MOMENTS AT POINTS (1) $ (2)
(eaction force @ disc%arge el"o! e6it = 7. 8026.30 kg
!"(!0.83 in-lb
Seismic force = 7s = mass 6 acceleration "39( lbf
8end#moment @ pt .due to seismic force =Ms,./ = 26(0( in-lb
8end#moment @ pt due to seismic force =Ms,/ = "8"3( in-lb
9om"ined "end#moment @ pt . = M. = M.,./ : Ms 980!(.83 in-lb
9om"ined "end#moment @ pt = M = M.,/ : Ms 89!0(.83 in-lb
Mean radius of run pipe = (m .!0! inch
Mean radius of saf valve nozzle @ pt . = r'm 2.!!3 inch
STRESS INTENSIFICATION FACTORS AT POINTS (1 )$ ( 2)
)uter radius of saf valve nozz @ pt . = rp .02 inch
3.3 -
Stress intensication factor for pt ,"utt !eld/ = i, ".00 -
kg/cm2
inch4
Safety valve installation period = * = ;#. 6 ?,$
8ending moment @ pt . due to force7.=M.,./ M.,/ = 7. A 1 A D17
= i,./ = ,,(m4*r/B45/6,r'm4(m/B;#C 6 ,*'"4 *r/ 6,r'm4rp/
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Safety valve nozzle M/S.CETHAR VESSELS (P ) LTDM/S.BINANI CEMENTS
PREDICTED STRESSES AT POINT (1) - BRANCH CONNECTION
(atio = Do4 *r for run pipe 8.0( -
(atio = dn.4 *'" for safety valve nozzle 3.23003800( -
ts = lesser of *r or ,i./*'" " inch
r" = r'm 2.!!3 inch
Section modulus of point ,./ =.= r"B ts 32.00
Pressure stress,./ for "ranc% conn# =Ps,./ 8282.30 psi
000.63 psi
PREDICTED STRESSES AT POINT (2) - BUTT %ELD
(atio = dn.4 tn for safety valve nozzle 3.26 -
9.!9
Pressure stress,/ for "utt !eld =Ps,/ 33(!. psi
7actor ;#FC 6 i,/ 0.!( -
" -
983(.2" psi
COMPARISON OF PREDICTED STRESS %ITH ALLO%ABLE STRESS
3ncrease factor for %ot allo!a"le stress = + ".20 -
llo!a"le %ot stress @ design temp = + 6 S% 2"80.00 psi
8322.93 psi
"3"92.6 psi
9om" stress,./ condition c%ec+ 9s,./ G= ,+ 6 S%/ NOT SAFE -
9om" stress,/ condition c%ec+ 9s, /G= ,+ 6 S%/ SAFE -
inch3
7le6ure stress,./ for "ranc% connection =7s,./=,;#FC6 i,./6 M,.//4 ,./
,dnB- diB/4dn inch3
ta+en as .#;
7le6ure stress,/ for "utt !eld =7s,/=,;#FC6 i,/6 M,//4 ,/
9om"ined stress at point ,./ "ranc% conn = 9s,./=Pr#stress Ps,./ :7le6#stress 7s,./
9om"ined stress at point ,/ "utt !eld =9s,/ =Pr#stress Ps,/ : 7le6#stress 7s,/
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Safety valve nozzle M/S.CETHAR VESSELS (P ) LTDM/S.BINANI CEMENTS
Date:-02-09-06Rev:-00 .
Prepared by Verified by Approved by .
SAFETY VALVE NOZZLE DESIGN CALCULATION AS PER ASME B31.1-2010
Description I!"# Unit
Safety valve set pressure = P 2!0.30
Design temperature (!3.60 °C
Nozzle material specication SA"82 #"2$%2 -
Young's Modulus of material @ design temp = E 2.8&'0! psi llo!a"le stress for saf#valve nozz#matl @ design te 000.00 psi
$eig%t of valve = $ 22.00 kgs
Nozzle %eig%t from od of run pipe = & 200.00 mm
Dist# "et!# od of run pipe to centre line outlet pipe (20.00 mm
(un pipe outside diameter =)#D 2!3.00 mm
*%ic+ness of run pipe = *r 3."0 mm
Saf# valve nozz#od @ pipe conn ,point-./ = dn.#=rp "8.20 mm
Saf# valve nozz#t%+ @pipe conn ,point-./ = *'"# (9.60 mm
Saf# valve nozz#od @ valve conn ,point-/ = dn# "8.20 mm
Saf# valve nozz#t%+ @ valve conn ,point-/ = tn# (8.80 mm
0alve rise time = to 0.0 sec
Moment arm = 1 6"0.00 mm
Moment arm for point ,./ =1. 20 inch
Moment arm for point ,/ =1 "3 inch
Seismic coe2cient ".( -
verage od of saf#valve nozzle = do !.2(2 inch
verage id of saf#valve nozzle = di 2.(6 inch
Moment of inertia of saf#valve nozzle = 3 "33.66
0.0090(8 sec
(atio = to4 * .2 -
Dynamic load factor ,g 33#5# of ap6#-33 of asme "5. "."( -
BENDING MOMENTS AT POINTS (1) $ (2)
(eaction force @ disc%arge el"o! e6it = 7. 929!.! kg
(6(9(0.3" in-lb
Seismic force = 7s = mass 6 acceleration "39( lbf
8end#moment @ pt .due to seismic force =Ms,./ = 2!900 in-lb
8end#moment @ pt due to seismic force =Ms,/ = "8"3( in-lb
9om"ined "end#moment @ pt . = M. = M.,./ : Ms (938(0.3" in-lb
9om"ined "end#moment @ pt = M = M.,/ : Ms (808(.3" in-lb
Mean radius of run pipe = (m .!03 inch
Mean radius of saf valve nozzle @ pt . = r'm 2.(3 inch
STRESS INTENSIFICATION FACTORS AT POINTS (1 )$ ( 2)
)uter radius of saf valve nozz @ pt . = rp 3.63 inch
2.9( -
Stress intensication factor for pt ,"utt !eld/ = i, ".00 -
PREDICTED STRESSES AT POINT (1) - BRANCH CONNECTION
(atio = Do4 *r for run pipe 8.0" -
(atio = dn.4 *'" for safety valve nozzle 3.090600268 -
ts = lesser of *r or ,i./*'" " inch
r" = r'm 2.(3 inch
kg/cm2
inch4
Safety valve installation period = * = ;#. 6 ?,$
8ending moment @ pt . due to force7.=M.,./ M.,/ = 7. A 1 A D17
= i,./ = ,,(m4*r/B45/6,r'm4(m/B;#C 6 ,*'"4 *r/ 6,r'm4rp/
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Safety valve nozzle M/S.CETHAR VESSELS (P ) LTDM/S.BINANI CEMENTS
Date:-02-09-06Rev:-00 .
Prepared by Verified by Approved by .
Section modulus of point ,./ =.= r"B ts 2(.00
Pressure stress,./ for "ranc% conn# =Ps,./ !692.9! psi
(2(((.!( psi
PREDICTED STRESSES AT POINT (2) - BUTT %ELD
(atio = dn.4 tn for safety valve nozzle 3."3 -
36.86
Pressure stress,/ for "utt !eld =Ps,/ 30"0.22 psi
7actor ;#FC 6 i,/ 0.!( -
" -
"(8(."2 psi
COMPARISON OF PREDICTED STRESS %ITH ALLO%ABLE STRESS
3ncrease factor for %ot allo!a"le stress = + ".20 -
llo!a"le %ot stress @ design temp = + 6 S% 800.00 psi
6028.!2 psi
"88((.3 psi
9om" stress,./ condition c%ec+ 9s,./ G= ,+ 6 S%/ NOT SAFE -
9om" stress,/ condition c%ec+ 9s, /G= ,+ 6 S%/ NOT SAFE -
inch3
7le6ure stress,./ for "ranc% connection =7s,./=,;#FC6 i,./6 M,.//4 ,./
,dnB- diB/4dn inch3
ta+en as .#;
7le6ure stress,/ for "utt !eld =7s,/=,;#FC6 i,/6 M,//4 ,/
9om"ined stress at point ,./ "ranc% conn = 9s,./=Pr#stress Ps,./ :7le6#stress 7s,./
9om"ined stress at point ,/ "utt !eld =9s,/ =Pr#stress Ps,/ : 7le6#stress 7s,/
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Safety valve nozzle M/S.CETHAR VESSELS (P ) LTDM/S.BINANI CEMENTS
Date:-02-09-06Rev:-00 .
Prepared by Verified by Approved by .
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Safety valve nozzle M/S.CETHAR VESSELS (P ) LTDM/S.BINANI CEMENTS
Date:-02-09-06Rev:-00 .
Prepared by Verified by Approved by .
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)*)+A)DA,*R
Rle/ for te de/i1n of /aftey valve in/tallation
a Design pressure and velocity
P inlet pre//re Ab/olte 92( p/i
, 4nlet te5pereatre "000
At5o/peri pre//re "( psia
W 7ei1t of te valve 800 lb #ro5 SV data /eet
Valve openin1 ti5e 0.0 sec #ro5 SV data /eet
Di/ar1e elbo area (0.03
ravitational on/tant 32.2
"(0!.30 Btu/lbm #ro5 /tea5 table/
j on/tant !!8."6 Btu/lbm
W Atal 5a// flo rate ""6.38 lbm/sec
Pre//re te di/ar1e elbo ""8 psia
Veloity te di/ar1e elbo 2""6 ft/sec
B Discharge Elbow max operating pressur
#or 8 in. la// "(0 AS+& 7eld ne; flan1e
% in H ,14D/ =D !.98" in 32.00
% ".6!
% "2
D !.98" "9 p/ia
%
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D Bending Moment at points (1 and (!
(A!
@ F1 " # " $#F
# 5o5ent ar5 2.00 in
$F# Dyna5i load fator "."" fro5 1rap
%o Fin& $F#
' )oungs mo&ulus of inlet pipe * &esign t 23000000 Psi
"9 in
+ ,oment of inetia of inlet pipe
*D 9.8!( in
4D 6 in
+ 03
Ben&ing moment , 0.00( sec
#or a valve ri/e ti5e
300!.23 in-lb
(A!
Aeleration ".( Data fron /trtre
5a// aeleration
"200 lbf
5o5ent ar5 for point " "9 in
22800 in-lb
5o5ent ar5 for point 2 "2 in
"00 in-lb
(c!
36320!.23 in-lb
3(80!.23 in-lb
Ben&ing moment at the point (1! . (2! &ue to ecation at point (1!
,1(1!
,1(2!
h &istance fom un pipe to centeline ofoutlet piping
in
,1(1!
,1(2!
,1(1!
,1(2!
Ben&ing moment at the point (1! . (2! &ue to eismicloa&ing
F s
F s
,(1!
,(2!
Ben&ing moment at the point (1! . (2! &ue to eismicloa&ing
,(1!
,1(1!
' ,(1!
,(2!
,1(2!
' ,(2!
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/tea5 ondition a> Bt000
p/ia
/pereated
/tea5 F 90 Eality "000 p/ia Gp" G 2>000 p/ia
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823
.33
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