P [psia] 4000T [R] 620R [psia*ft3]/[lbmol*R] 10.732

Componentes Pc [psia] Tc [R] Tr Xi YiC1 667 343.34 1.8058 0.45 0.86C2 706.6 549.92 1.1274 0.05 0.05C3 615.5 665.92 0.9310 0.05 0.05C4 550.9 765.55 0.8099 0.03 0.02C5 488.8 845.8 0.7330 0.01 0.01C6 436.9 913.8 0.6785 0.01 0.005

C7+ 285 1160 0.5345 0.4 0.0051 1

LQUIDO (X)

Xi (C1) Xi (C2) Xi (C3) Xi (C4) Xi (C5)1210.25 242.59 335.84 257.69 105.00242.59 48.63 67.32 51.65 21.05335.84 67.32 93.20 71.51 29.14257.69 51.65 71.51 54.87 22.36105.00 21.05 29.14 22.36 9.11124.31 24.92 34.50 26.47 10.798965.99 1797.20 2488.05 1909.08 777.87

11241.67 2253.35 3119.54 2393.63 975.30

GAS (Y)

Yi (C1) Yi (C2) Yi (C3) Yi (C4) Yi (C5)4420.25 463.62 641.83 328.32 200.66463.62 48.63 67.32 34.44 21.05641.83 67.32 93.20 47.67 29.14328.32 34.44 47.67 24.39 14.90200.66 21.05 29.14 14.90 9.11118.79 12.46 17.25 8.82 5.39214.19 22.46 31.10 15.91 9.72

6387.66 669.97 927.50 474.45 289.98

Ecuacin Cbica de Soave-Riedlich-Kwong : Z3- Z2+(A-B-B2)*Z - AB = 0

w a m b0.0115 8701.4162 0.4981 0.6868 0.47860.0994 21071.3502 0.6347 0.9231 0.72360.1529 35471.7838 0.7165 1.0509 1.00600.2003 52377.0843 0.7882 1.1640 1.29210.2515 72056.1632 0.8647 1.2642 1.60890.2993 94099.4818 0.9353 1.3570 1.94480.52 232454.5694 1.2509 1.7859 3.7845

Xi (C6) Xi (C7+)124.31 8965.9924.92 1797.2034.50 2488.05 A26.47 1909.08 B10.79 777.87 Ecuacin Cbica12.77 920.96 Z1920.96 66423.44 Z2

1154.71 83282.58 Z3

Yi (C6) Yi (C7+)118.79 214.1912.46 22.4617.25 31.10 A8.82 15.91 B5.39 9.72 Ecuacin Cbica3.19 5.76 Z15.76 10.38 Z2

171.66 309.52 Z3

Ecuacin Cbica de Soave-Riedlich-Kwong : Z3- Z2+(A-B-B2)*Z - AB = 0

Densidad Lquido [lb/ft3](a)m bm

Densidad Gas [lb/ft3](a)mbm

Xi*bi Yi*bi PM PM*Xi PM*Yi0.2154 0.4116 16 7.2 13.760.0362 0.0362 30 1.5 1.50.0503 0.0503 44 2.2 2.20.0388 0.0258 58 1.74 1.160.0161 0.0161 72 0.72 0.720.0194 0.0097 86 0.86 0.431.5138 0.0189 215 86 1.0751.8900 0.5687 100.22 20.85

42.658290799 Z f(x)104420.79177 0 -10.7188

1.8900 Coeficientes 0.2 -9.34949.4341389025 a 1 0.4 -8.01201.1361723735 b -1 0.6 -6.6586

0.00004 c 7.0071 0.8 -5.24111.4123 d -10.7188 1 -3.7117

imaginaria 1.2 -2.0223imaginaria 1.4 -0.1249

1.6 2.0285

13.518190326 Z f(x)9230.73 0 -0.28510.5687 Coeficientes 0.2 -0.2421

0.8339721709 a 1 0.4 -0.23100.3418653248 b -1 0.6 -0.2040

-0.00001 c 0.3752 0.8 -0.11290.9270 d -0.2851 1 0.0901

imaginaria 1.2 0.4532imaginaria 1.4 1.0242

1.6 1.8513

2)*Z - AB = 0

f(x)

f(x)

f(x)

P [psia] 4000T [R] 620R [psia*ft3]/[lbmol*R] 10.732

Componentes Pc [psia] Tc [R] Tr Xi YiC1 667 343.34 1.8058 0.45 0.86C2 706.6 549.92 1.1274 0.05 0.05C3 615.5 665.92 0.9310 0.05 0.05C4 550.9 765.55 0.8099 0.03 0.02C5 488.8 845.8 0.7330 0.01 0.01C6 436.9 913.8 0.6785 0.01 0.005

C7+ 285 1160 0.5345 0.4 0.0051 1

LQUIDO (X)

Xi (C1) Xi (C2) Xi (C3) Xi (C4) Xi (C5)1294.53 259.48 359.23 275.64 112.31259.48 52.01 72.01 55.25 22.51359.23 72.01 99.69 76.49 31.17275.64 55.25 76.49 58.69 23.91112.31 22.51 31.17 23.91 9.74132.97 26.65 36.90 28.31 11.549313.50 1866.85 2584.48 1983.07 808.02

11747.67 2354.77 3259.96 2501.37 ###

GAS (Y)

Yi (C1) Yi (C2) Yi (C3) Yi (C4) Yi (C5)4728.09 495.90 686.53 351.18 214.64495.90 52.01 72.01 36.83 22.51686.53 72.01 99.69 50.99 31.17351.18 36.83 50.99 26.08 15.94214.64 22.51 31.17 15.94 9.74127.06 13.33 18.45 9.44 5.77222.49 23.34 32.31 16.53 10.10

6825.89 715.93 991.14 507.00 309.87

Ecuacin Cbica de PENG-ROBINSON : Z3+(B-1)*Z2+(A-3B2-2B)*Z - (AB-B2-B3) = 0

w a m b0.0115 9307.4029 0.4981 0.6868 0.42980.0994 22538.8078 0.6347 0.9231 0.64980.1529 37942.1209 0.7165 1.0509 0.90330.2003 56024.7456 0.7882 1.1640 1.16030.2515 77074.3212 0.8647 1.2642 1.44480.2993 100652.7875 0.9353 1.3570 1.74630.52 248643.2435 1.1074 1.6843 3.3984

Xi (C6) Xi (C7+)132.97 9313.5026.65 1866.8536.90 2584.48 A28.31 1983.07 B11.54 808.02 Ecuacin Cbica13.66 956.66 Z1956.66 67005.71 Z2

1206.69 84518.28 Z3

Yi (C6) Yi (C7+)127.06 222.4913.33 23.3418.45 32.31 A9.44 16.53 B5.77 10.10 Ecuacin Cbica3.41 5.98 Z15.98 10.47 Z2

183.44 321.21 Z3

Ecuacin Cbica de PENG-ROBINSON : Z3+(B-1)*Z2+(A-3B2-2B)*Z - (AB-B2-B3) = 0

Densidad Lquido [lb/ft3](a)m bm

Densidad Gas [lb/ft3](a)mbm

Xi*bi Yi*bi PM PM*Xi PM*Yi0.1934 0.3696 16 7.2 13.760.0325 0.0325 30 1.5 1.50.0452 0.0452 44 2.2 2.20.0348 0.0232 58 1.74 1.160.0144 0.0144 72 0.72 0.720.0175 0.0087 86 0.86 0.431.3594 0.0170 215 86 1.0751.6971 0.5107 100.22 20.85

47.567830246 Z f(x)106607.93014 0 -7.72387

1.6971 Coeficientes 0.2 -6.821369.6317409977 a 1 0.4 -5.869221.0202471221 b 0.020247 0.6 -4.81946

0.00014 c 7.5706 0.8 -3.624091.2666 d -11.9296 1 -2.23509

imaginaria 1.2 -0.60448imaginaria 1.4 1.31576

1.6 3.57361

14.082344054 Z f(x)9854.48 0 -0.150150.5107 Coeficientes 0.2 -0.17114

0.8903254594 a 1 0.4 -0.199570.3069843291 b -0.693016 0.6 -0.18745

0.00005 c -0.0064 0.8 -0.086770.88985 d -0.1501 1 0.15048

imaginaria 1.2 0.57228imaginaria 1.4 1.22664

1.6 2.16156

+(A-3B2-2B)*Z - (AB-B2-B3) = 0

f(x)

f(x)

f(x)

P [psia] 3990T [R] 610R [psia*ft3]/[lbmol*R] 10.732

Componentes Pc [psia] Tc [R] Tr Xi YiC1 667 343.34 1.7767 0.41 0.84C2 706.6 549.92 1.1093 0.06 0.06C3 615.5 665.92 0.9160 0.06 0.06C4 550.9 765.55 0.7968 0.04 0.02C5 488.8 845.8 0.7212 0.02 0.01C6 436.9 913.8 0.6675 0.01 0.005

C7+ 285 1160 0.5259 0.4 0.0051 1

LQUIDO (X)

Xi (C1) Xi (C2) Xi (C3) Xi (C4) Xi (C5)1017.84 268.48 371.61 316.77 193.61268.48 70.82 98.02 83.56 51.07371.61 98.02 135.67 115.65 70.69316.77 83.56 115.65 98.59 60.25193.61 51.07 70.69 60.25 36.83114.61 30.23 41.85 35.67 21.808267.99 2180.91 3018.59 2573.17 1572.70

10550.92 2783.09 3852.08 3283.66 2006.94

GAS (Y)

Yi (C1) Yi (C2) Yi (C3) Yi (C4) Yi (C5)4272.38 550.06 761.34 324.50 198.33550.06 70.82 98.02 41.78 25.53761.34 98.02 135.67 57.83 35.34324.50 41.78 57.83 24.65 15.06198.33 25.53 35.34 15.06 9.21117.41 15.12 20.92 8.92 5.45211.74 27.26 37.73 16.08 9.83

6435.77 828.59 1146.86 488.81 298.76

Ecuacin Cbica de Soave-Riedlich-Kwong : Z3- Z2+(A-B-B2)*Z - AB = 0

w a m b0.0115 8701.4162 0.4981 0.6959 0.47860.0994 21071.3502 0.6347 0.9336 0.72360.1529 35471.7838 0.7165 1.0624 1.00600.2003 52377.0843 0.7882 1.1764 1.29210.2515 72056.1632 0.8647 1.2777 1.60890.2993 94099.4818 0.9353 1.3716 1.94480.52 232454.5694 1.2509 1.8058 3.7845

Xi (C6) Xi (C7+)114.61 8267.9930.23 2180.9141.85 3018.59 A35.67 2573.17 B21.80 1572.70 Ecuacin Cbica12.91 931.02 Z1931.02 67161.59 Z2

1188.10 85705.98 Z3

Yi (C6) Yi (C7+)117.41 211.7415.12 27.2620.92 37.73 A8.92 16.08 B5.45 9.83 Ecuacin Cbica3.23 5.82 Z15.82 10.49 Z2

176.86 318.96 Z3

Ecuacin Cbica de Soave-Riedlich-Kwong : Z3- Z2+(A-B-B2)*Z - AB = 0

Densidad Lquido [lb/ft3](a)m bm

Densidad Gas [lb/ft3](a)mbm

Xi*bi Yi*bi PM PM*Xi PM*Yi0.1962 0.4020 16 6.56 13.440.0434 0.0434 30 1.8 1.80.0604 0.0604 44 2.64 2.640.0517 0.0258 58 2.32 1.160.0322 0.0161 72 1.44 0.720.0194 0.0097 86 0.86 0.431.5138 0.0189 215 86 1.0751.9171 0.5764 101.62 21.27

43.086505 Z f(x)109370.76017 0 -11.8979

1.9171 Coeficientes 0.2 -10.400110.182469744 a 1 0.4 -8.93441.1684657069 b -1 0.6 -7.4527

0.00091 c 7.6487 0.8 -5.90691.4375 d -11.8979 1 -4.2492

imaginaria 1.2 -2.4314imaginaria 1.4 -0.4057

1.6 1.8760

14.2081279 Z f(x)9694.61 0 -0.31710.5764 Coeficientes 0.2 -0.2635

0.9025729449 a 1 0.4 -0.24190.3513085196 b -1 0.6 -0.2044

0.00014 c 0.4278 0.8 -0.10280.9122 d -0.3171 1 0.1108

imaginaria 1.2 0.4843imaginaria 1.4 1.0659

1.6 1.9035

2)*Z - AB = 0

f(x)

f(x)

f(x)

P [psia] 3990T [R] 610R [psia*ft3]/[lbmol*R] 10.732

Componentes Pc [psia] Tc [R] Tr Xi YiC1 667 343.34 1.7767 0.41 0.84C2 706.6 549.92 1.1093 0.06 0.06C3 615.5 665.92 0.9160 0.06 0.06C4 550.9 765.55 0.7968 0.04 0.02C5 488.8 845.8 0.7212 0.02 0.01C6 436.9 913.8 0.6675 0.01 0.005

C7+ 285 1160 0.5259 0.4 0.0051 1

LQUIDO (X)

Xi (C1) Xi (C2) Xi (C3) Xi (C4) Xi (C5)1088.72 287.18 397.49 338.83 207.09287.18 75.75 104.85 89.38 54.63397.49 104.85 145.12 123.71 75.61338.83 89.38 123.71 105.45 64.45207.09 54.63 75.61 64.45 39.39122.60 32.34 44.76 38.15 23.328584.26 2264.33 3134.06 2671.60 1632.86

11026.18 2908.45 4025.59 3431.57 2097.34

GAS (Y)

Yi (C1) Yi (C2) Yi (C3) Yi (C4) Yi (C5)4569.92 588.37 814.36 347.10 212.14588.37 75.75 104.85 44.69 27.31814.36 104.85 145.12 61.85 37.80347.10 44.69 61.85 26.36 16.11212.14 27.31 37.80 16.11 9.85125.59 16.17 22.38 9.54 5.83219.84 28.30 39.18 16.70 10.21

6877.32 885.44 1225.54 522.35 319.26

Ecuacin Cbica de PENG-ROBINSON : Z3+(B-1)*Z2+(A-3B2-2B)*Z - (AB-B2-B3) = 0

w a m b0.0115 9307.4029 0.4981 0.6959 0.42980.0994 22538.8078 0.6347 0.9336 0.64980.1529 37942.1209 0.7165 1.0624 0.90330.2003 56024.7456 0.7882 1.1764 1.16030.2515 77074.3212 0.8647 1.2777 1.44480.2993 100652.7875 0.9353 1.3716 1.74630.52 248643.2435 1.1074 1.7013 3.3984

Xi (C6) Xi (C7+)122.60 8584.2632.34 2264.3344.76 3134.06 A38.15 2671.60 B23.32 1632.86 Ecuacin Cbica13.81 966.64 Z1966.64 67684.35 Z2

1241.61 86938.10 Z3

Yi (C6) Yi (C7+)125.59 219.8416.17 28.3022.38 39.18 A9.54 16.70 B5.83 10.21 Ecuacin Cbica3.45 6.04 Z16.04 10.58 Z2

189.00 330.84 Z3

Ecuacin Cbica de PENG-ROBINSON : Z3+(B-1)*Z2+(A-3B2-2B)*Z - (AB-B2-B3) = 0

Densidad Lquido [lb/ft3](a)m bm

Densidad Gas [lb/ft3](a)mbm

Xi*bi Yi*bi PM PM*Xi PM*Yi0.1762 0.3610 16 6.56 13.440.0390 0.0390 30 1.8 1.80.0542 0.0542 44 2.64 2.640.0464 0.0232 58 2.32 1.160.0289 0.0144 72 1.44 0.720.0175 0.0087 86 0.86 0.431.3594 0.0170 215 86 1.0751.7215 0.5176 101.62 21.27

48.085795464 Z f(x)111668.85123 0 -8.65235

1.7215 Coeficientes 0.2 -7.6433510.396423113 a 1 0.4 -6.582401.0492455216 b 0.049246 0.6 -5.42151

0.00013 c 8.2463 0.8 -4.112691.2880 d -13.1644 1 -2.60792

imaginaria 1.2 -0.85922imaginaria 1.4 1.18143

1.6 3.56201

14.850280163 Z f(x)10349.75 0 -0.17306

0.5176 Coeficientes 0.2 -0.185620.963566847 a 1 0.4 -0.20495

0.3154640215 b -0.684536 0.6 -0.183040.00006 c 0.0341 0.8 -0.071890.87276 d -0.1731 1 0.17649

imaginaria 1.2 0.61011imaginaria 1.4 1.27697

1.6 2.22507

+(A-3B2-2B)*Z - (AB-B2-B3) = 0

f(x)

0 0.2 0.4 0.6 0.8 1 1.2 1.4 1.6 1.8-0.5

0.0

0.5

1.0

1.5

2.0

2.5

f(x)

0 0.2 0.4 0.6 0.8 1 1.2 1.4 1.6 1.8-0.5

0.0

0.5

1.0

1.5

2.0

2.5

f(x)

SWK-CLASE (1)PENG-ROBINSON-CLASE (1)SWK-TALLER (2)PENG-ROBINSON-TALLER (2)