TALLER 1
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Ci % Mol Yi GPM GPM % Recobro N2 0.298 0.00298 0 0.033 - Co2 8.234 0.08234 0 1.393 - C1 .881 0.881 0 11.310 - C2 12.12 0.1212 0 3.233 - C3 !."21 0.0!"21 2.04 9 iC4 1.229 0.01229 0.401 98 nC4 2.148 0.02148 0.!" 98 iC" 0."41 0.00"41 0.19! 99 nc" 0.484 0.00484 0.1!" 99 C 0.301 0.00301 0.123 100 C! 0.149 0.00149 0.09 100 C8 0.01 0.0001 0.031 100 C9 0.01! 0.0001! 0.01 100 C10 0.00! 0.0000! 0.0043 100 C11# 0.003 0.00003 0.0023 100 ∑ 100 1 3.752 PCN$% 1.00E#0 Resues!as se u&ica 'e(e)ente *or enci)a de 'os 1000 +tu$*cn. 1." Corriente de gas )u, rico. 2." La reduccion de' (a'or de' gas sera de 1.1"0.090 3." E' gas cu)*'e con 'as es*ecicacion de *oder ca'
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Taller Venta de Gas y Liquidos
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Ci % Mol Yi GPM GPM % Recobro
N2 0.298 0.00298 0 0.033 -
Co2 8.234 0.08234 0 1.393 -C1 .881 0.881 0 11.310 -
C2 12.12 0.1212 0 3.233 -
C3 !."21 0.0!"21 2.04 9
iC4 1.229 0.01229 0.401 98
nC4 2.148 0.02148 0.!" 98
iC" 0."41 0.00"41 0.19! 99
nc" 0.484 0.00484 0.1!" 99
C 0.301 0.00301 0.123 100
C! 0.149 0.00149 0.09 100
C8 0.01 0.0001 0.031 100
C9 0.01! 0.0001! 0.01 100
C10 0.00! 0.0000! 0.0043 100
C11# 0.003 0.00003 0.0023 100
∑ 100 1 3.752
PCN$% 1.00E#0
Resues!as
se u&ica 'e(e)ente *or enci)a de 'os 1000 +tu$*cn.
1." Corriente de gas )u, rico.
2." La reduccion de' (a'or de' gas sera de 1.1"0.090
3." E' gas cu)*'e con 'as es*ecicacion de *oder ca'
7/17/2019 TALLER 1
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Universidad del Zulia
Postgrado Ingenieria en Gas
Extraccion de Liquidos
Gal#dia $!raer Gas a &en!a Mol#dia Yi Residuo
- 32!00.8 !8"2.44 0.0034
- 1393329.3 219!".414 0.0941- 1130919. 1!2391.31 0.!40
- 32333".! 319"34.112 0.138"
1.98144 0.082" 0.008 3.43E-09
0.39298 0.00802 0.001 2.81E-10
0.1" 0.013" 0.001 4.90E-10
0.19"03 - - -
0.1!32" - - -
0.123 - - -
0.09 - - -
0.031 - - -
0.01 - - -
0.0043 - - -
0.0023 - - -
3.'(( 15)')015.( 230'753.*1 1
8!".4E#
educc / 100012"88 - 8!"391018 312 38189 PCN$%
Reducc + 11500)0 ,-lar#dia
Pao'ares *or dia.
rico ,a que e' de (enta o residua'
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% Molar Gas a &en!a //& !u#c li !u#c Resid
0.34 0 0 0
9.41 0 0 0!.40 1010 !"."0 !!1."
13.8" 1!9.! 214."9 24".14
0.00 2"1.2 189.24 0.00
0.00 32"2 39.9! 0.00
0.00 322.4 !0.08 0.00
- 4000.9 21.4"
- 4008.! 19.402
- 4!" 14.31
- ""02." 8.199
- 248.9 3.812
- 99.4 1.189
- !!43 0."42
- 8942 0.28
100.00 125*.* 101'.*
lo Cincilla &"1'11)')*
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5 6 Grossetano 1.04 1010
Et7ane 30.0! 1!9.!
Pro*ane 44.1 2"1
I-+utane "8.12 32"2
n-+utane "8.12 322
I-Pentane !2.1" 4001
n-Pentane !2.1" 4009
n-exane 8.1!" 4!"
n-e*tane 100.202 ""03
n-ctane 114.229 249n-Nonane 128.2"" 99!
n- %ecane 142.282 !!43
undecano 1".312
100
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00
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900
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,/ "329!1"312#111!
;+ *)(2
0 20 40 0 80 100 120 140 100
0
0
0
0
0
0
0
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:x / "3.29"292928x # 11.1893390!; / 0.99999"94"1
C6 ,$ /$4G &8U$ GR6 U,$C6
Molecular 9ei:!
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