140-P-005 With Calculated DP ISO-final
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user Input
1쪽
put data for Stream
eam No.
kg/h
Volume m3/h
ss Flowrate for Case study kg/h
nsity kg/m3
cosity cp
mperature ℃
ecular !eight
ecific heat ratio Cp/C"
minal #ipe Si$e in
ut %nside Diameter in
h. No.
aight &ength m
ui"alent &ength )*y +ser, m
ughness m
ut &ine #ress. Drop kg/cm
tation of Velocity
tation of #ress. Drop
mber of Fittings (Mode1)
gate/*all/plug ea
glo*e ea
*utterfly ea
check ea
0 el*o ea
12 el*o ea
ee *ranch ea
ee through ea
m
put Data for Device
scription
ssure kg/cm)g,
ssure Drop kg/cm
"ation m
er Design for CV 4
ase &/V/Mi5ed
wrate Mass
mpress.Fact. 6
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put data for Pump
No.
erencial #ressure kg/cm
nter 'le"ation m
por #ressure kg/cm)a,
ut7ff #ressure kg/cm
Factor
rmal # press at Suction kg/cm)g,
From '& to 8&& mDri"e ype )Motor/ur*ine,
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)CV e(n 9 :D Manual e(uation, ;:arometric # 9 <.0<3 *ar= 8ydroMaster V3.
<rev 0 : 24-11-09 ><rev 1 : 2010-05-10 > Z:\Persona !o"ers
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)CV e(n 9 :D Manual e(uation, ;:arometric # 9 <.0<3 *ar= 8ydroMaster V3.
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'D "ata 29,4++ 29,4++
v name F'D-442 F'D-442
v P1 +,125 +,125
v P2 5,0*3 5,0*3
v !oG 12))+2,+00 12))+2,+00
v "ens )31,200 )31,200
'v vaue 114,0*0 114,0*0
P%ase $Cu$" $Cu$"
oop 1,000 3,000
over "es$gn 1,000 1,000
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45쪽
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54쪽
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55쪽
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Jo* No 9 #C0?3#roKect Name 9 Malaysian lefin #roKect
EGo p%ase stream ana@s$s date 9 0</02/0<#age <10 of <10
Stream for# .est t/o pase stream ana2sis(%0-3-1%%4 1% IN53.) prepared *y 9 :..%M
Process Data First Point Reference Pointflowrate pres temp mw density "isco Cp 8 "ap # 6 pres temp density "isco Cp 8 "ap # 6
kg/h *ar)a, ℃ kg/m3 cp kcal/kgC kcal/kg *ar)a, factor *ar)a, ℃ kg/m3 cp kcal/kgC kcal/kg *ar)a, factor
VAP 2?.2 @.1 72?.< 33.0 0.00?@ <. 000.00 @.3?0 <.00 @.3?0 72?.00 <2.<0 0.00?@ <. <00.00 1.000 <.00
LIQ <0<<.2 13.@@0 0.03 .3 13.@@0 0.03 .3
Geometry Datano element desc diameter length rough angle -/D D/D< 7"alue no element desc diameter length rough angle -/D D/D< 7"alue
in m m in m m
< pipe <<< 1 < 0.000<2 0 <<
*end *ara 1 0.000<2 0 <.200 <
3 <3
1 <1
2 <2 <
? <?
@ <@
<
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Calclation !t"t
no eement desc engt ange 6 press temp void 7uait2 densit2 veocit2 ma8" ve fo/ pattern Pressure Drop (bar9m) bar
m vaue bar(a) # fraction :g9m m9s m9s ; < regime friction gravit2 moment .ota
1 start 0.00 0 @.1<0 72?.<0 0.33< 0.02 332.33 <.0? 0.00'L0
% pipe <<< <.00 0 @.3? 72?.<0 0.33 0.02 331.2 <.0? 0.0 .2'L 2.<'L0 *u*slg .2'71 3.3'7 2.?'7 3.32'7
*end *ara 3.@ 0.000 @.3?2 72?.<0 0.3< 0.02 31<.3 <.02 0.0 1.<'71 0.0'L0 ?.0'7@ <.2?'73
0.00'L0
' 0.00'L0
0.00'L0
Fr
or
E
87
hori$ontal flowaitel and DuklerE <?
8B A annular dispersed li(uid8: A dispersed *u**le8C A stratified wa"y8D A stratified smooth>3 ? intermittent (sug and pug)
DOQ
DO
"ertical upward flow 8ewitt and -o*ertsE <
V+B A annular
V+: A wispy annular
$@C ? curn$@D ? bubb2 sugV+' A *u**le
D=Q
D=
"ertical downward flowolan and StenningE <
$DA ? annuar $DB ? osciar2VDC A slug and *u**le
1.2 1.6 2.0
1.6
1.2
0.8
0.4
0
0 0.4 0.8
VDA
VDB
VDC
2.0
VUA
1000
100
10
1
0.1
1 10 100 1000 10000 100000
VUB
VUC
VUD
VUE
10000
1000
10
1
0.1
0.01
0.001
0.001 0.01 0.1 1 10 100 1000 10000
HAHB
HEHC HD
10000
100
10
1