gpsa - gas processors suppliers association, engineering 12th ed (excel)

8/15/2019 GPSA - Gas Processors Suppliers Association, Engineering 12th Ed (Excel)

1/19

Liquid Vol

Component mole fraction (x) MW x•MW

Caron !ioxide "#""$$ %%#"$ "#"%&%$$

Met'ane "#"2$% $#"%3 "#3%332"2

t'ane "#3&9* 3"#"* $$#*$&2*9

+ropane "#3%& %%#"9* $#"&,&,.o-utane "#"29% ,$23 $#*"&&$2

/ormal-utane "#"&** ,$23 ,#"9*3&*$

.o-pentane "#"$*$ *2#$, $#233*,

/ormal-pentane "#"$&2 *2#$, $#3$3$3

0exane. 1 "#"*" &*#%3 #$*29&$

4L $ %3#*22*,*

5i6en7 otal p


2/19

page 23-9

me Fraction Calculation

ma.. fraction (M) lm F5# 23-2 (lm:gal) gal 6

"#""$$"*22&* 9$3#*9,&2 #&$99 $33#9&922 "#""",$3,

"#""*&,2223 %&"#%39, 2#, 2,92#$*,& "#"$2"$$,

"#2&"$3* 22$$9$#*2 2#99 *%%&,#3*23 "#32"9"$9

"#3*923$*3 3"3%#99, %#22& *$&3,",, "#3%9223$*"#"39"&3",, 322,,#2,% %#92* &*3#%9,&, "#"33%$3$

"#$$,&%,$& 92$*#2"32 %#&9$ $9*"#***& "#"9"$

"#"2&2$*9, 232&&*& ,#2",& %%*3#,2*$& "#"2$*%&2

"#"3""33$,*% 2%*&#3%& ,#2$% %*$"#9&2*& "#"229"$$,

"#$%$$&%9""$ $$,$9#&9& ,#,9$ 2"&%"#$&, "#$"$3$"9,

$ &2,3"" 2",*"9#%%, $

und. ma.. 8 &2,3"" Lm


3/19

.pecific 6olume (V)$#,

Fig# 2%-2* f(+)

den.it; (-factor "#93,9*"**,


4/19

page 23-$$

+ure Component +ropertie.

lm:ft3

?F

p.ia

ft3:lm @=A 9$ equation

(p.ia ft3):(?= lmol)


5/19


6/19

Calculatio

F5# 23-2

Component

C0% "#&3$9 -$$#

C20 "#"&%& &9#92C30& "#"%3* 2",#92

iC%0$" "#""* 2*%#%$

nC%0$" "#"$& 3",#,,

iC,0$2 "#"",* 39

nC,0$2 "#""32 3&,#&

nC0$% "#""3 %,3#&

4L $

MoleFraction

;i

ComponentCritical

emperatureci ?F


7/19

page 23-$$

n of +.eudo-critical emperature and +re..ure for a /atural 5a. Mixture

F5# 23-2

3%2#"$ 2&%#,$&$$9 #% ,,%#3*&$

,%,9 %#,2"%32 *"#, ,9#9$$2%#,9 29#"%2,&3 $ 2#9$92

*33#"& ,#,*$%"& ,2*#9 %#"$2"%

*%#22 $2#&3&&9 ,,"# 9#2,""&

&2*#* %#*$**$9 %9"#% 2#*9,2&

&%%#%* 2#*"23"% %& $#,3,2

9$2#%* ,#*%&,$ %3#9 2#*,2%*

pc 8 +pc8

39$#""22 $#,&$9,

.pecific gra6it; o

ComponentCritical

emperatureci ?=

+.eudocriticalemperature

pc ?=

ComponentCritical

+re..ure+ci p.ia

+.eudocritical+re..ure+pc p.ia


8/19

F5# 23-2

$#"%3 $3#3%$*$*

3"#"* 2#,%993%%#"9* $#92*"3&9

,$23 "#%%$*3%&

,$23 "#9*%%

*2#$, "#%$$2,,

*2#$, "#23"&&

&#$** "#,%29$,$

MWm8

2"#%239*9

r relati6e den.it; (ga. den.it;)

5 8

"#*"3"9&$3

ComponentMolecular Weig't

MW

MixtureMolecular

Weig't;i •MW


9/19

page 23-$*

!etermine t'e >-factor for t'e

Component

02@ "#2

C2 "#"*

$"" ?F

+ $""" p.ia#

c %33#9 ?=

+c &2#9 p.ia

o eFraction


10/19

.our natural ga.

B 29#& ?F Fig# 23-&

c %"%#$ ?=

+c *$#*3&%* p.ia

$#3&%9*&9*$#3$2*&,3

> "#&3$ Fig# 23-%

r

+r


11/19


12/19

page 23-3

Calculation of Vi.co.it; of a 5a

F5# 23-2 F5# 23-2

Component

"#& $#"%3 $2#&3%% *

"#$, 2"$3 %#2"$9, %92#&

"#", %%#"$ 2#2"", $"9#,

$ $9#23&,

MoleFraction

;i

ComponentMolecular

Weig'tMW


MW

ComponentCritical

+re..ure+ci p.ia

C0%

/2

C2


13/19

. Mixture

F5# 23-2 F5# 23-2

-$$# 3%2#"$ 2*3#"& "#"9&& $#,&,"%&% $#2&"3&*2

-232#,3 22#$% 33#92$ "#",$ $#%2&3 "#2$%299%,

&*#* ,%#%3 2*#32$, "#"3%2 $#,",$%2 "#"*,2,*$

33%#&,", $#,,*,9,2*

ComponentCritical

emperatureci ?F

ComponentCritical

emperatureci ?=

ComponentCritical

emperatureci ?=

Vci

ft3:l

Vci

ft3:l mole

Vci

ft3:l mole


14/19

"#2&&"9$$ "#23"%*2&*

"#29"$,",% "#"%3,22,&$%

"#2*%,,$2 "#"$3*2*,&"9

"#2&**23"3&9

>ci

ft3:l

>ci

ft3:l


15/19

page 23-2%

Calculation of Liquid !en.it; of a Mixt

F5# 23-2 F5# 23-2

Component Weig't l

Met'ane "#2"&9 $#"%3 3#3,23%,2&

Caron !ioxide "#39*3 %%#"$ $*#%&,$*3 "#&22"3

t'ane "#"$&& 3"#"* "#,*$2"2+ropane "#"23&* %%#"9* $#",2,9,39 "#,"*3&

n-Dutane "#"3,& ,$23 2#"&%29"*& "#,&%"&

n-+entane "#"2%%* *2#$, $#*,,$", "#3$$3

n-0exane "#"$&%% &#$** $#,&9$"3&& "#%"%

n-0eptane "#"29&3 $""#2"% 2#9&9"&,32 "#&&$9

n-ctane "#"299, $$%#23$ 3#%2$2$&%, "#*"9&

n-!ecane "#$&2"& $%2#2&, 2,#9"*2,2& "#*3%"

n-etradecane "#"3"3& $9'% #"2*2"9*2

4L $

MoleFraction

;i


MW

=elati6e den.it;of liquid "?F


16/19

re at $2"?F and $*" p.ia

=eference.

LudEig. 4pplied +roce.. !e.ign for C'emic

" 4 "#22&2*

,$#22&9"9 &9,#*%3%* D "#2*2%

" 2&*",, A 3$#$992$ 33#2&29&3* %2,#$& A

3#399&, *,#&*9"%3 n "#2&3

39#332"2$ 9#%%$"9*$ den.it; "#,&39%92 g:mL

%$#3&29*2& ,#*$&%2 den.it; 3#%39%$"* l:cu ft

%2#&&&"""& $2$9,&9%

%%#",&993 $,"#*3,%%2

%,#*%$92 $$&,#$923

%*#&$, 2&$9$"33

!en.it; ("?F)l:cu ft

Volumecu ft

C


17/19

al and +etroc'emical +lant.

4ppendix C

4ppendix C

4ppendix C

4ppendix C


18/19

page 2%-$"

xample nt'alp;

F5# 23-2 F5# 23-2

Component

Met'ane "#9"$ $#"%3 -$$# 3%2#"$

Caron !ioxide "#"$" %%#"$ &*#9 ,%#,*

t'ane "#"%99 3"#"* &9#92 ,%,9

+ropane "#"$&* %%#"9* 2",#92 %#,9

i-Dutane "#"", ,$23 2*%#%$ *33#"&

n-Dutane "#""%, ,$23 3",#,, *%#22

i-+entane "#""$* *2#$, 39 &2*#*

n-+entane "#""$9 *2#$, 3&,#& &%%#%*

0exane "#"",2 &#$** %,3#& 9$2#%*

4L $ MWm8

2",,#%

MoleFraction

;i

ComponentMolecular

Weig'tMW

ComponentCritical

emperatureci ?F

ComponentCritical

emperatureci ?=


19/19

Calculation

F5# 23-2 F5# 23-2G

3"$,$"$ * ""#9* "#"$"& 292

,#*93%2 $"9#, $$#33* "#2* $""

2*#3*%%$ *"#, 3,#2,%3, "#"9*2 $&9

$2#%2*&33 $ $$#,$92 "#$,$, $2

%#*,"2 ,2*#9 3#%3$3, "#$&,2 $,$

3#%3&99 ,,"# 2#%*** "#$9&$ $2

$#%"*"39 %9"#% "#&33& "#22& $,$

$#"%%93 %& "#92&3% "#2,$ $,&

%#*%%&%% %3#9 2#2*$&& "#299 $39

pc 8 +pc8

39#*"*,$2 9#"2"2

+.eudocriticalemperature

pc ?=

ComponentCritical

+re..ure+ci p.ia

+.eudocritical+re..ure+pc p.ia

4centricFactor

deal 5a.nt'alp;

Dtu:l

gpsa - gas processors suppliers association, engineering 12th ed (excel)

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