140-P-005 With Calculated DP ISO-final

7/23/2019 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



user Input

2쪽

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,



)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

1,052-1#'

0,33#'

0,+

0

0

<107C700

S7002

0.010 *ar 0.<0 m

<107#7002B/:1.00 *ar

0.<0 m

F'711

0.20 *ar 0.200 m

FCV711

0.000 *ar 0.200 m )GH9 0.0

<107'B7003

89 / V9 0.220 *ar

89 / V9 <@.220 m

<107''700?

S9 0.<10 / 9 *ar S9 <.20 / 9 m

<107C7007N<0

?.300 *ar)g,

<.000 m

S#7<

0.000 *ar

0.<0 m

'700B/:/C/DS9 0.?20 / 9 *ar

S9 3.?00 / 9 m

-712

0.000 *ar

<.000 m

31 2

<?<@

<1

<107V70<

89 / V9 <.000 *ar

89 / V9 <.200 m

<0 <<

V700

89 0.?00 / V9 *ar

89 2.000 / V9 m

1, ;/7 Pressure o! 5 .arg $s assume" to .e at t%e gr$",

2, 'auate" =P !or 8?s are prorate" as per t%e pump apa$t@

3, Pump sut$on an" &tream 5A*A9 B 10 C, 7engt% $s .ase" on$sometr$s

4, 140-D-009 Eop evat$on $s assume" to .e 5m,

<

<107C7007N0?

?.300 *ar)g,

.000 m

sp73

0.000 *ar

0.<0 m

?

S#

0.000 *ar

<@.200 m

@

S#20.000 *ar <@.200 m

F$ter

;akGas%

<

<3

S#2

0.000 *ar

1.200 m

# down;*ar)g,=

d# head;*ar=

&ine si$e;in=

Flowrate;kg/h=

Density;kg/m3=

Viscosity;cp=

Velocity;m/s=

Stra. &ength;m=

'(u". &ength;m=

d# "ari.;*ar=

phase

Stream no

Flowrate;m3/h=

d# "ari;*ar/<00m=

?.2

70.310

<

<0.20

<<0@.<

@<.200

0.200

<.3<<.10

13.?0

0.0<

li(uid

3.3?

0.03

?.<

0.000

<0.20

<@@?.?0

@<.200

0.200

0.1.30

<@.<0

0.001

li(uid

<@.<0

0.03

?.2@0

0.000

3

<0.00

<@@?<.2

@<.200

0.200

<.030.@0

.0

0.00<

li(uid

<@.<0

0.0

<<.??

0.000

1

.02

<@@?<.2

@<.200

0.200

[email protected]

<2.00

0.02

li(uid

<@.<0

0.31

<<.2

0.<@?

2

.02

<@@?<.2

@3.100

0.200

.@<32.00

0.0

0.3<2

li(uid

<@@.2?

0.31@

.01

<.<2

.02

<@@?<.2

[email protected]

0.?00

.1<1.00

@.0

0.?2

li(uid

<<.12

0.30

.030

0.001

?

.02

113.00

[email protected]

0.?00

<.03.00

.00

0.00?

li(uid

@0.?3

0.0@0

@.1??

70.001

@

.02

113.00

@<.00

<.2000

<.<@3.00

.00

0.00?

li(uid

?@.<

0.0@<

@.@?

70.20<

.02

<@@?<.2

@<.00

<.2000

.32<3.00

3.@0

0.<0<

li(uid

<2?.@<

0.30

.0?

70.2

<0

.02

<@@?<.2

@3.300

.3000

.3<<@.00

3@.@0

0.<<

li(uid

<21.@1

0.3<

@.@

70.@2

<<

.02

<@@?.?0

@3<.000

.1000

.3<<0.00

30.00

0.01

li(uid

<22.0@

0.3<1

?.<1

0.12

<

.02

<@@?.?0

@3<.00

.1000

.3<?0.00

<02.00

0.330

li(uid

<22.01

0.3<1

?.103

70.3

<3

.02

<@@?.?0

@3<.00

.1000

.3<<0.00

<2.00

0.01?

li(uid

<22.01

0.3<1

?.<2

0.000

<1

.02

<@@?.?0

@3<.00

.1000

.3<3.00

.00

0.0@

li(uid

<22.01

0.3<1

1.<

0.3

<2

.02

<@@?.?0

@3<.00

.1000

.3<@.00

1.00

0.0?2

li(uid

<22.01

0.3<1

<@

@

li(



)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\#m

1,052- 1#'

0,33#'

0,+

0

0

Shu

'& t

Dri"e

<107C700

S70020.010 *ar

0.<0 m

<107#7002B/:

1.00 *ar 0.<0 m

F'7110.20 *ar

0.200 m

FCV7110.000 *ar

0.200 m )GH9 0.0 4,

<107'B7003

89 / V9 0.220 *ar

89 / V9 <@.220 m

<107''700?S9 0.<10 / 9 *ar

S9 <.20 / 9 m

<107C7007N<0

?.300 *ar)g,

<.000 m

S#7<

0.000 *ar

0.<0 m

'700B/:/C/D

S9 0.?20 / 9 *ar

S9 3.?00 / 9 m

-712

0.000 *ar <.000 m

31 2

<?<@

<1

<107V70<

89 / V9 <.000 *ar

89 / V9 <.200 m

<0 <<

V700

89 0.?00 / V9 *ar

89 2.000 / V9 m

<2

S#7

0.00

1.20

1, ;/7 Pressure o! 5 .arg $s assume" to .e at t%e gr$",

2, 'auate" =P !or 8?s are prorate" as per t%e pump apa$t@

3, Pump sut$on an" &tream 5A*A9 B 10 C, 7engt% $s .ase" on$sometr$s

<

<107C7007N0?

?.300 *ar)g,

.000 m

sp73

0.000 *ar 0.<0 m

?

S#

0.000 *ar

<@.200 m

@

S#20.000 *ar

<@.200 m

F$ter ;akGas%<

<3

S#20.000 *ar

1.200 m

# down;*ar)g,=

d# head;*ar=

&ine si$e;in=

Flowrate;kg/h=

Density;kg/m3=

Viscosity;cp=

Velocity;m/s=

Stra. &ength;m='(u". &ength;m=

d# "ari.;*ar=

phase

Stream no

Flowrate;m3/h=

d# "ari;*ar/<00m=

2.000

70.3?

<

.02

<@@?.?0

@3<.00

.1000

.3<

3.00.00

0.0@

li(uid

<22.01

0.3<1



auat$on

5쪽

'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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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 <

? <?

@ <@

<

<0 0

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

Documents

140-P-005 With Calculated DP ISO-final