Calculo de Gpm

7/23/2019 Calculo de Gpm

http://slidepdf.com/reader/full/calculo-de-gpm 1/11

ANALISIS CROMATOGRAFICO PROMEDIO ENERO - SEPTIEMBRE/2007

GAS DE EXPORTACION AL BRAZIL

Componentes Pome!"o M#n"mo M$%"mo

Hexano 0.08 0.07 0.09

Propano 1.87 1.77 1.95

Iso- Butano 0.28 0.26 0.29

Normal-Butano 0.4 0.37 0.42

Neo-Pentano 0 0 0

Iso-Pentano 0.11 0.1 0.12

Normal-Pentano 0.07 0.06 0.08

≤ 2,00% mol 1.46 1.39 1.56

Etano 6.25 6.05 6.38

Oxígeno ≤ 0,20 % mol 0.01 0.01 0.01

Nitrógeno ≤ 2,00% mol 0.74 0.69 0.8

Metano 88.74 88.54 89.03

Tot&' (00

Poder Calorífico (BT!PC" (0)7*7+ 1044.49 1050.35

#ra$edad &'ecífica 0*,,. 0.63406 0.63828

Pre&i) *+e&ra (P&i-" 1200

Tem'era+ra m+e&ra (/" 94

P (P&ia" 2000

/ (mole& oale& de la m+e&ra"

(/raccio) li+ido, mole&", $alor a&+mido 0.0000002

(/racci) $a'or, mole&" 0.9999998

i (mole& del com'o)e)e i e) la m+e&ra

i (/racci) molar del com'o)e)e i e) la fa&e $a'or de la m+e&ra"

i (/racci) molar del com'o)e)e i e) la fa&e lí+ida de la m+e&ra"

Ca+dal de a& (***C" 30

Ca+dal de a& (*PC" 1059440

#P* de cada com'o)e)e

Espe""&"ones

C6:C

3

i;C4

);C4

)eo;C5

i;C5

);C5

Dióxido de

Carbono C<2

C2

<2

=2

C1

> 1034 B+!f3

0,590 ≤ ?#≤ 0,690

Contenido de Líquido de cada componente GPM = ∑ 2.63410Contenido de Líquido de cada componente GPM = ∑ 2.63410



Z" 1" 3Z" 4 1"5 3Z" / 1"5

@2<

=2 0.007400 0.007400 5.570 0.041218 0.00132855 0.001328546

C<2 0.014600 0.014600 1.530 0.022338 0.00954248 0.0095424843

C1 0.887400 0.887400 2.450 2.174130 0.36220408 0.3622041245

C2 0.062500 0.062500 0.820 0.051250 0.07621951 0.0762195088

C3 0.018700 0.018700 0.363 0.006788 0.05151515 0.0515151334

iC4 0.002800 0.002800 0.203 0.000568 0.0137931 0.0137930926

)C4 0.004000 0.004000 0.650 0.002600 0.00615385 0.0061538455

iC5 0.001100 0.001100 0.095 0.000105 0.01157895 0.0115789253

)C5 0.000700 0.000700 0.076 0.000053 0.00921053 0.0092105039

)C6 0.000800 0.000800 0.028 0.000022 0.02857143 0.0285712302

Toal 1.000000 1.000000 11.785000 2.299073 0.570118 0.570117

Conten"!o !e GLP en 0 MMMCD !e 6&s !e e%pot&"n &' B&s"' 3en MCD5

Conten"!o !e G&so'"n& n&t8&' en 0 MMMCD !e 6&s !e e%pot&"n &' B&s"' 3e

9ERIFICACION DE LOS CALC:LOS POR OTROS M;TODO

C&'8'o !e' onten"!o !e '#<8"!o 3GLP = G&so'"n& N&t8&'5

M>to!o N? ( M>to!o N? 2

@2<

=2 0.007400 0 2.6341063 4.151

C<2 0.014600 0 2.6341063 6.453

C1 0.887400 0 2.6341063 6.417

C2 0.062500 0 2.6341063 10.148

C3 0.018700 27.4816 0.51390592 2.6341063 10.433

iC4 0.002800 32.626 0.0913528 2.6341063 12.386

)C4 0.004000 31.4433 0.1257732 2.6341063 11.937

iC5 0.001100 36.1189 0.03973079 2.6341063 13.853)C5 0.000700 36.1189 0.02528323 2.6341063 13.712

)C6 0.000800 41.0157 0.03281256 2.6341063 15.571

Toal 1.000000

#P 're&e)e e) el a& (&olo C3 );iC4", e) #al!*PC. 0*7(0*0@+

Compos""n

F&"nMo'& ="

xi = Zi/[L+

(V*Ki)]

Como '& Re'&"n 3Z"/1"5 es meno <8e 8no '& m8est& est$ en&se 6&seos&*

Compenentes

F&"nMo'&

F&to !eones"n

6&s &'#<8"!o

GPM 3G&'ones!e L#<8"!opo MPC !e

6&s5

Dens"!&! omo'#<8"!o G&'/L-

Mo'

#a&oli)a =a+ral e) el a& (Pe)a)o& &+'eriore&", e)#alo)e&!*PC.



#P e) el a& (&olo C3 );iC4", e) *3!**PC de a&. 2*7,72*#a&oli)a =a+ral e) el a& (Pe)a)o& &+'eriore&", e) BB!**PC

de a&.



3* Yi *ρ3* Yi *ρ iqiq



GPM de GLP

2.6341063

0.0073999932

0.0145999985

0.8873997427

0.0625000023

0.0187000024 10.433 0.514

0.0028000004 12.386 0.091

0.0040000003 11.938 0.126

0.0011000002 13.86 0.040

0.0007000001 13.714 0.025

0.0008000002 15.566 0.033

1.000000 0*7( 0*0@+

2@2BPD5 2)7+

S

0.0809187446

0.2481768557

15.000243058

1.6706819208

0.5139065002

0.0913529138

0.1257733076

0.0401393020.0252832059

0.0328125354 (.).A.T"!P

((1110.73520"!(14.7"" 379.6354

Como e& la ca)idad de li+ido e) mil 'i

1000!379.6354 2.6341063

0*7( 2.6341063

0*0@+

yi = Zi/[V+

(L*Ki)]

Dens"!&!omo

'#<8"!oG&'/L mo'

GPM deGasolinaNatural

GPM 3G&'ones!e L#<8"!o poMPC !e 6&s5

GLPI68&'es G&so'"n&

N&t8&'I68&'es



2*7,72*)

/acor de co)$er&io) a& a li+ido (de)&idad como li+ido!379,635

C3 (10,433!379,6354"1000 27,4816





e& c+ico& de a& e)emo&



"1000



Compos""n

Mo' Po"ento E""en"& !e Aso"n

Mo' 1

@2<

=2 1.683600 4.3000 0.063 0.0635

C<2 0.060900 1.8000 0.152 0.1517

C1 85.233400 3.1500 0.087 0.0867

C2 8.921300 0.9000 0.303 0.3032

C3 2.364500 0.3740 0.730 0.6965

iC4 0.303600 0.2100 1.300 0.9431

)C4 0.694500 0.1700 1.606 0.9772iC5 0.229300 0.0900 3.034 0.9991

)C5 0.232900 0.0740 3.689 0.9997

C6 0.146300 0.0350 7.801 1.0000

C7: 0.129700 0.0165 16.547 1.0000

Toal 100.000000

Con!""ones &s8m"!&s p&& e' ee""o=+mero de mole&!Dora de a& 100.00

l aceie a&ore)e 'ore )o ie)e )i)E) com'o)e)e del a& raado

alore& de F (+iliri+m Aaio" oe)ido de Tala& del #P?-

e /i+ra 19;48 oe)emo&G

a (ficie)cia de -&orci) (70 %" 0.70

=+mero de 'lao& 6

- (/acor de a&orci)" 0.73

Aelacio) de refl+Ho oG

27.30

=+mero de 'lao& ma& 1 7

1.00

Pre&i) (P&ia" 1200

Tem'era+ra (/" 100

E<8"'""8mR&t"o

F&to !eAso"on

ALo/1&64 9n(

E&3An( - A5/3An( - (5

o -(Fa$"():1", mole&!Dora

L& s8m&to"& !e 'os mo'es !e &!& omponente !e '& o"ente !e' 6&s poe <8e s&'em"ent&s <8e 'os mo'es !e &!& omponente <8e 8eon &o"!os po e' &e"te poe



1.577 0.11

0.052 0.01

77.846 7.39

6.216 2.70

0.718 1.65

0.017 0.29

0.016 0.680.000 0.23

0.000 0.23

0.000 0.15

0.000 0.13

+,*)) (*.,

Mo'es !e&!&

omponenteen e' 6&s

poe

C&8!&' !e L"<8"!oen Mo'es/Ho&

(33 n(5 -

(5/3 n(5 - 0L=(Yn+) ! Y + Y"

e '& &soe!o& es +,))en '& &soe!o& son(.,

Documents

Calculo de Gpm