termodinamica para ingenieria quimica ejercicio

18
Curso: Termodinámica de Ingeniería Química Profesor: Dr. Jorge Flores Franco Alumnos: Diego Pérez, Amilcar Vásquez Aguilar, Jessica Karen Vásquez Cerquera, Israel Roman Ciclo: Nivelación-2013 Fecha: 01 de Febrero del 2013 TRUJILLO – PERÙ FACULTAD DE INGENIERIA QUÍMICA Ejercicio 10.7

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Page 1: Termodinamica Para Ingenieria Quimica Ejercicio

Curso:

Termodinámica de Ingeniería Química

Profesor:

Dr. Jorge Flores Franco

Alumnos:

Diego Pérez, Amilcar

Vásquez Aguilar, Jessica Karen

Vásquez Cerquera, Israel Roman

Ciclo:

Nivelación-2013

Fecha:

01 de Febrero del 2013

TRUJILLO – PERÙ

2013

FACULTAD DE INGENIERIA QUÍMICA

E S C U E L A DE I N G E N I E R Í A QUÍMICA

Ejercicio 10.7

Page 2: Termodinamica Para Ingenieria Quimica Ejercicio

1

Solución con Iteraciones:

ln P1sat=13.8594− 2773.78

t+220.07

ln P2sat=14.0045− 3279.47

t+213.20

ln (α )= 3279.47t+213.20

− 2773.78t+220.07

−0.1451 ; α=P1sat

P2sat

P=P2sat+ (P1sat−P2sat ) x1

P1sat=P ( y1+ y2α )

Termodinámica de Ingeniería Química: Equilibrio Vapor Líquido

Una sola etapa de separación líquido/vapor para un sistema de benceno (1)/etilbenceno (2) debe producir fases para las siguientes composiciones de equilibrio. Para uno de estos conjuntos, determine la T y P en el separador. ¿Qué información adicional se necesita calcular para las cantidades relativas de líquido y vapor que salen del separador? Suponga que se aplica la ley de Raoult.

a) x1= 0.35, y1=0.70b) x1= 0.35, y1=0.725c) x1= 0.35, y1=0.75d) x1= 0.35, y1=0.775

EJERCICIO 10.7

Parámetros para la ecuación de AntoineSustancia A B CBenceno 13.8594 2773.78 220.07

Etilenceno 14.0045 3279.47 213.20

Page 3: Termodinamica Para Ingenieria Quimica Ejercicio

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a) x1= 0.35, y1=0.70

Asumimos T=135°C

Tsupuesta

ln(α) α lnP1

P1 lnP2 P2 P P1calculado

Tcalculado

135.00 1.46 4.31 6.05 423.04 4.59 98.12 211.84 422.30 134.92134.92 1.46 4.31 6.05 422.30 4.58 97.91 211.45 421.63 134.85134.85 1.46 4.31 6.04 421.63 4.58 97.71 211.08 421.00 134.78134.78 1.46 4.32 6.04 421.00 4.58 97.53 210.75 420.43 134.72134.72 1.46 4.32 6.04 420.43 4.58 97.37 210.44 419.90 134.66134.66 1.46 4.32 6.04 419.90 4.58 97.22 210.16 419.42 134.61134.61 1.46 4.32 6.04 419.42 4.58 97.08 209.90 418.97 134.56134.56 1.46 4.32 6.04 418.97 4.57 96.96 209.66 418.57 134.52134.52 1.46 4.32 6.04 418.57 4.57 96.84 209.44 418.19 134.48134.48 1.46 4.32 6.04 418.19 4.57 96.73 209.24 417.85 134.44134.44 1.46 4.32 6.04 417.85 4.57 96.64 209.06 417.53 134.40134.40 1.46 4.32 6.03 417.53 4.57 96.55 208.89 417.24 134.37134.37 1.46 4.33 6.03 417.24 4.57 96.46 208.73 416.97 134.34134.34 1.46 4.33 6.03 416.97 4.57 96.39 208.59 416.72 134.32134.32 1.46 4.33 6.03 416.72 4.57 96.32 208.46 416.50 134.29134.29 1.46 4.33 6.03 416.50 4.57 96.25 208.34 416.29 134.27134.27 1.47 4.33 6.03 416.29 4.57 96.19 208.23 416.10 134.25134.25 1.47 4.33 6.03 416.10 4.57 96.14 208.12 415.92 134.23134.23 1.47 4.33 6.03 415.92 4.57 96.09 208.03 415.76 134.21134.21 1.47 4.33 6.03 415.76 4.56 96.04 207.94 415.61 134.20134.20 1.47 4.33 6.03 415.61 4.56 96.00 207.86 415.47 134.18134.18 1.47 4.33 6.03 415.47 4.56 95.96 207.79 415.35 134.17134.17 1.47 4.33 6.03 415.35 4.56 95.93 207.72 415.23 134.15134.15 1.47 4.33 6.03 415.23 4.56 95.89 207.66 415.12 134.14134.14 1.47 4.33 6.03 415.12 4.56 95.86 207.60 415.03 134.13134.13 1.47 4.33 6.03 415.03 4.56 95.83 207.55 414.94 134.12134.12 1.47 4.33 6.03 414.94 4.56 95.81 207.50 414.85 134.11134.11 1.47 4.33 6.03 414.85 4.56 95.79 207.46 414.78 134.11134.11 1.47 4.33 6.03 414.78 4.56 95.76 207.42 414.71 134.10134.10 1.47 4.33 6.03 414.71 4.56 95.74 207.38 414.64 134.09134.09 1.47 4.33 6.03 414.64 4.56 95.73 207.35 414.58 134.08134.08 1.47 4.33 6.03 414.58 4.56 95.71 207.32 414.53 134.08134.08 1.47 4.33 6.03 414.53 4.56 95.69 207.29 414.48 134.07134.07 1.47 4.33 6.03 414.48 4.56 95.68 207.26 414.43 134.07134.07 1.47 4.33 6.03 414.43 4.56 95.67 207.24 414.39 134.06134.06 1.47 4.33 6.03 414.39 4.56 95.65 207.21 414.35 134.06134.06 1.47 4.33 6.03 414.35 4.56 95.64 207.19 414.32 134.06134.06 1.47 4.33 6.03 414.32 4.56 95.63 207.17 414.28 134.05

Termodinámica de Ingeniería Química: Equilibrio Vapor Líquido

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134.05 1.47 4.33 6.03 414.28 4.56 95.62 207.16 414.25 134.05134.05 1.47 4.33 6.03 414.25 4.56 95.62 207.14 414.23 134.05134.05 1.47 4.33 6.03 414.23 4.56 95.61 207.12 414.20 134.04134.04 1.47 4.33 6.03 414.20 4.56 95.60 207.11 414.18 134.04134.04 1.47 4.33 6.03 414.18 4.56 95.59 207.10 414.16 134.04134.04 1.47 4.33 6.03 414.16 4.56 95.59 207.09 414.14 134.04134.04 1.47 4.33 6.03 414.14 4.56 95.58 207.08 414.12 134.03134.03 1.47 4.33 6.03 414.12 4.56 95.58 207.07 414.10 134.03134.03 1.47 4.33 6.03 414.10 4.56 95.57 207.06 414.09 134.03134.03 1.47 4.33 6.03 414.09 4.56 95.57 207.05 414.07 134.03134.03 1.47 4.33 6.03 414.07 4.56 95.56 207.04 414.06 134.03134.03 1.47 4.33 6.03 414.06 4.56 95.56 207.03 414.05 134.03134.03 1.47 4.33 6.03 414.05 4.56 95.56 207.03 414.04 134.02134.02 1.47 4.33 6.03 414.04 4.56 95.55 207.02 414.02 134.02134.02 1.47 4.33 6.03 414.02 4.56 95.55 207.02 414.02 134.02134.02 1.47 4.33 6.03 414.02 4.56 95.55 207.02 414.02 134.02

T=134.02°C y P=207.02 kPa

b) x1= 0.35, y1=0.725

Asumimos T=115°C

tsupuesta

ln(α) α lnP1 P1 lnP2

P2 P P1calculado t calculado

115.00 1.57 4.80 5.58 265.39 4.01 55.27 128.81 263.48 114.71114.71 1.57 4.81 5.57 263.48 4.00 54.78 127.82 261.75 114.44114.44 1.57 4.82 5.57 261.75 4.00 54.34 126.93 260.17 114.20114.20 1.57 4.82 5.56 260.17 3.99 53.93 126.12 258.74 113.98113.98 1.57 4.83 5.56 258.74 3.98 53.57 125.38 257.44 113.77113.77 1.58 4.84 5.55 257.44 3.97 53.24 124.71 256.25 113.59113.59 1.58 4.84 5.55 256.25 3.97 52.93 124.09 255.17 113.42113.42 1.58 4.85 5.54 255.17 3.96 52.66 123.54 254.19 113.26113.26 1.58 4.85 5.54 254.19 3.96 52.41 123.03 253.30 113.12113.12 1.58 4.85 5.53 253.30 3.95 52.18 122.57 252.48 112.99112.99 1.58 4.86 5.53 252.48 3.95 51.98 122.15 251.74 112.88112.88 1.58 4.86 5.53 251.74 3.95 51.79 121.77 251.07 112.77112.77 1.58 4.86 5.53 251.07 3.94 51.62 121.43 250.45 112.67112.67 1.58 4.87 5.52 250.45 3.94 51.46 121.11 249.89 112.58112.58 1.58 4.87 5.52 249.89 3.94 51.32 120.82 249.38 112.50112.50 1.58 4.87 5.52 249.38 3.94 51.19 120.56 248.92 112.43112.43 1.58 4.87 5.52 248.92 3.93 51.07 120.32 248.49 112.36112.36 1.58 4.88 5.52 248.49 3.93 50.96 120.10 248.11 112.30112.30 1.58 4.88 5.51 248.11 3.93 50.87 119.90 247.75 112.24

Termodinámica de Ingeniería Química: Equilibrio Vapor Líquido

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112.24 1.58 4.88 5.51 247.75 3.93 50.78 119.72 247.43 112.19112.19 1.59 4.88 5.51 247.43 3.93 50.70 119.55 247.14 112.14112.14 1.59 4.88 5.51 247.14 3.92 50.62 119.40 246.87 112.10112.10 1.59 4.88 5.51 246.87 3.92 50.56 119.27 246.63 112.06112.06 1.59 4.88 5.51 246.63 3.92 50.49 119.14 246.40 112.02112.02 1.59 4.89 5.51 246.40 3.92 50.44 119.03 246.20 111.99111.99 1.59 4.89 5.51 246.20 3.92 50.39 118.92 246.02 111.96111.96 1.59 4.89 5.51 246.02 3.92 50.34 118.83 245.85 111.93111.93 1.59 4.89 5.50 245.85 3.92 50.30 118.74 245.69 111.91111.91 1.59 4.89 5.50 245.69 3.92 50.26 118.66 245.55 111.89111.89 1.59 4.89 5.50 245.55 3.92 50.22 118.59 245.42 111.86111.86 1.59 4.89 5.50 245.42 3.92 50.19 118.52 245.31 111.85111.85 1.59 4.89 5.50 245.31 3.92 50.16 118.46 245.20 111.83111.83 1.59 4.89 5.50 245.20 3.91 50.13 118.41 245.10 111.81111.81 1.59 4.89 5.50 245.10 3.91 50.11 118.36 245.01 111.80111.80 1.59 4.89 5.50 245.01 3.91 50.09 118.31 244.93 111.78111.78 1.59 4.89 5.50 244.93 3.91 50.07 118.27 244.86 111.77111.77 1.59 4.89 5.50 244.86 3.91 50.05 118.23 244.79 111.76111.76 1.59 4.89 5.50 244.79 3.91 50.03 118.20 244.73 111.75111.75 1.59 4.89 5.50 244.73 3.91 50.02 118.17 244.67 111.74111.74 1.59 4.89 5.50 244.67 3.91 50.00 118.14 244.62 111.73111.73 1.59 4.89 5.50 244.62 3.91 49.99 118.11 244.58 111.73111.73 1.59 4.89 5.50 244.58 3.91 49.98 118.09 244.53 111.72111.72 1.59 4.89 5.50 244.53 3.91 49.97 118.06 244.49 111.71111.71 1.59 4.89 5.50 244.49 3.91 49.96 118.04 244.46 111.71111.71 1.59 4.89 5.50 244.46 3.91 49.95 118.03 244.43 111.70111.70 1.59 4.89 5.50 244.43 3.91 49.94 118.01 244.40 111.70111.70 1.59 4.89 5.50 244.40 3.91 49.93 117.99 244.37 111.69111.69 1.59 4.89 5.50 244.37 3.91 49.92 117.98 244.35 111.69111.69 1.59 4.89 5.50 244.35 3.91 49.92 117.97 244.32 111.69111.69 1.59 4.90 5.50 244.32 3.91 49.91 117.96 244.30 111.68111.68 1.59 4.90 5.50 244.30 3.91 49.91 117.95 244.28 111.68111.68 1.59 4.90 5.50 244.28 3.91 49.90 117.94 244.27 111.68111.68 1.59 4.90 5.50 244.27 3.91 49.90 117.93 244.25 111.67111.67 1.59 4.90 5.50 244.25 3.91 49.89 117.92 244.24 111.67111.67 1.59 4.90 5.50 244.24 3.91 49.89 117.91 244.22 111.67111.67 1.59 4.90 5.50 244.22 3.91 49.89 117.91 244.21 111.67111.67 1.59 4.90 5.50 244.21 3.91 49.88 117.90 244.20 111.67111.67 1.59 4.90 5.50 244.20 3.91 49.88 117.89 244.19 111.66111.66 1.59 4.90 5.50 244.19 3.91 49.88 117.89 244.18 111.66111.66 1.59 4.90 5.50 244.18 3.91 49.88 117.88 244.17 111.66

T=111.66°C y P=117.89 kPa

Termodinámica de Ingeniería Química: Equilibrio Vapor Líquido

Page 6: Termodinamica Para Ingenieria Quimica Ejercicio

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c) x1= 0.35, y1=0.75

Asumimos T=90°C

tsupuesta ln(α) α lnP1 P1 lnP2 P2 P P1calculado t calculado90.00 1.73 5.61 4.91 136.15 3.19 24.25 63.41 136.57 90.1190.11 1.72 5.61 4.92 136.57 3.19 24.34 63.62 136.96 90.2190.21 1.72 5.61 4.92 136.96 3.20 24.43 63.81 137.31 90.3090.30 1.72 5.60 4.92 137.31 3.20 24.50 63.99 137.63 90.3890.38 1.72 5.60 4.92 137.63 3.20 24.57 64.14 137.92 90.4590.45 1.72 5.60 4.93 137.92 3.20 24.64 64.29 138.18 90.5190.51 1.72 5.60 4.93 138.18 3.21 24.70 64.42 138.42 90.5790.57 1.72 5.59 4.93 138.42 3.21 24.75 64.53 138.63 90.6390.63 1.72 5.59 4.93 138.63 3.21 24.80 64.64 138.83 90.6890.68 1.72 5.59 4.93 138.83 3.21 24.84 64.74 139.01 90.7290.72 1.72 5.59 4.93 139.01 3.21 24.88 64.82 139.17 90.7690.76 1.72 5.59 4.94 139.17 3.22 24.91 64.90 139.31 90.8090.80 1.72 5.58 4.94 139.31 3.22 24.95 64.97 139.44 90.8390.83 1.72 5.58 4.94 139.44 3.22 24.97 65.04 139.56 90.8690.86 1.72 5.58 4.94 139.56 3.22 25.00 65.10 139.67 90.8990.89 1.72 5.58 4.94 139.67 3.22 25.03 65.15 139.77 90.9190.91 1.72 5.58 4.94 139.77 3.22 25.05 65.20 139.86 90.9390.93 1.72 5.58 4.94 139.86 3.22 25.07 65.24 139.94 90.9590.95 1.72 5.58 4.94 139.94 3.22 25.08 65.28 140.01 90.9790.97 1.72 5.58 4.94 140.01 3.22 25.10 65.32 140.07 90.9990.99 1.72 5.58 4.94 140.07 3.22 25.11 65.35 140.13 91.0091.00 1.72 5.58 4.94 140.13 3.22 25.13 65.38 140.19 91.0291.02 1.72 5.58 4.94 140.19 3.22 25.14 65.41 140.24 91.0391.03 1.72 5.58 4.94 140.24 3.22 25.15 65.43 140.28 91.0491.04 1.72 5.58 4.94 140.28 3.23 25.16 65.45 140.32 91.0591.05 1.72 5.58 4.94 140.32 3.23 25.17 65.47 140.36 91.0691.06 1.72 5.57 4.94 140.36 3.23 25.18 65.49 140.39 91.0791.07 1.72 5.57 4.94 140.39 3.23 25.18 65.51 140.42 91.0791.07 1.72 5.57 4.94 140.42 3.23 25.19 65.52 140.45 91.0891.08 1.72 5.57 4.94 140.45 3.23 25.20 65.54 140.47 91.0991.09 1.72 5.57 4.95 140.47 3.23 25.20 65.55 140.49 91.0991.09 1.72 5.57 4.95 140.49 3.23 25.21 65.56 140.51 91.1091.10 1.72 5.57 4.95 140.51 3.23 25.21 65.57 140.53 91.1091.10 1.72 5.57 4.95 140.53 3.23 25.22 65.58 140.55 91.1191.11 1.72 5.57 4.95 140.55 3.23 25.22 65.59 140.56 91.1191.11 1.72 5.57 4.95 140.56 3.23 25.22 65.59 140.58 91.1191.11 1.72 5.57 4.95 140.58 3.23 25.23 65.60 140.59 91.1291.12 1.72 5.57 4.95 140.59 3.23 25.23 65.61 140.60 91.1291.12 1.72 5.57 4.95 140.60 3.23 25.23 65.61 140.61 91.1291.12 1.72 5.57 4.95 140.61 3.23 25.23 65.62 140.62 91.1291.12 1.72 5.57 4.95 140.62 3.23 25.24 65.62 140.63 91.1391.13 1.72 5.57 4.95 140.63 3.23 25.24 65.62 140.64 91.13

Termodinámica de Ingeniería Química: Equilibrio Vapor Líquido

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91.13 1.72 5.57 4.95 140.64 3.23 25.24 65.63 140.64 91.1391.13 1.72 5.57 4.95 140.64 3.23 25.24 65.63 140.65 91.1391.13 1.72 5.57 4.95 140.65 3.23 25.24 65.63 140.65 91.1391.13 1.72 5.57 4.95 140.65 3.23 25.24 65.64 140.66 91.1391.13 1.72 5.57 4.95 140.66 3.23 25.24 65.64 140.66 91.1391.13 1.72 5.57 4.95 140.66 3.23 25.25 65.64 140.67 91.1491.14 1.72 5.5

74.95 140.67 3.23 25.2

565.65 140.67 91.14

91.14 1.72 5.57

4.95 140.67 3.23 25.25

65.65 140.67 91.14

91.14 1.72 5.57

4.95 140.67 3.23 25.25

65.65 140.67 91.14

T=91.14°C y P=65.65 kPa

d) x1= 0.35, y1=0.775

Asumimos T=71°C

tsupuesta ln(α) α lnP1

P1 lnP2 P2 P P1calculado t calculado

71.00 1.86 6.45 4.33 75.93 2.47 11.77 34.22 76.22 71.1171.11 1.86 6.45 4.33 76.22 2.47 11.82 34.36 76.47 71.2271.22 1.86 6.44 4.34 76.47 2.47 11.87 34.48 76.70 71.3171.31 1.86 6.44 4.34 76.70 2.48 11.91 34.59 76.91 71.3971.39 1.86 6.43 4.34 76.91 2.48 11.96 34.69 77.10 71.4771.47 1.86 6.43 4.35 77.10 2.48 11.99 34.78 77.27 71.5471.54 1.86 6.43 4.35 77.27 2.49 12.02 34.86 77.42 71.6071.60 1.86 6.42 4.35 77.42 2.49 12.05 34.93 77.56 71.6571.65 1.86 6.42 4.35 77.56 2.49 12.08 35.00 77.68 71.7071.70 1.86 6.42 4.35 77.68 2.49 12.10 35.05 77.79 71.7471.74 1.86 6.42 4.35 77.79 2.50 12.12 35.11 77.89 71.7871.78 1.86 6.41 4.36 77.89 2.50 12.14 35.15 77.98 71.8271.82 1.86 6.41 4.36 77.98 2.50 12.16 35.20 78.06 71.8571.85 1.86 6.41 4.36 78.06 2.50 12.18 35.23 78.13 71.8871.88 1.86 6.41 4.36 78.13 2.50 12.19 35.27 78.19 71.9071.90 1.86 6.41 4.36 78.19 2.50 12.20 35.30 78.25 71.9271.92 1.86 6.41 4.36 78.25 2.50 12.21 35.33 78.30 71.9471.94 1.86 6.41 4.36 78.30 2.50 12.22 35.35 78.35 71.9671.96 1.86 6.40 4.36 78.35 2.50 12.23 35.37 78.39 71.9871.98 1.86 6.40 4.36 78.39 2.50 12.24 35.39 78.43 71.9971.99 1.86 6.40 4.36 78.43 2.51 12.25 35.41 78.47 72.0172.01 1.86 6.40 4.36 78.47 2.51 12.26 35.43 78.50 72.0272.02 1.86 6.40 4.36 78.50 2.51 12.26 35.44 78.52 72.0372.03 1.86 6.40 4.36 78.52 2.51 12.27 35.46 78.55 72.0472.04 1.86 6.40 4.36 78.55 2.51 12.27 35.47 78.57 72.0572.05 1.86 6.40 4.36 78.57 2.51 12.28 35.48 78.59 72.06

Termodinámica de Ingeniería Química: Equilibrio Vapor Líquido

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72.06 1.86 6.40 4.36 78.59 2.51 12.28 35.49 78.61 72.0672.06 1.86 6.40 4.36 78.61 2.51 12.28 35.50 78.62 72.0772.07 1.86 6.40 4.36 78.62 2.51 12.29 35.50 78.64 72.0772.07 1.86 6.40 4.36 78.64 2.51 12.29 35.51 78.65 72.0872.08 1.86 6.40 4.37 78.65 2.51 12.29 35.52 78.66 72.0872.08 1.86 6.40 4.37 78.66 2.51 12.29 35.52 78.67 72.0972.09 1.86 6.40 4.37 78.67 2.51 12.30 35.53 78.68 72.0972.09 1.86 6.40 4.37 78.68 2.51 12.30 35.53 78.69 72.1072.10 1.86 6.40 4.37 78.69 2.51 12.30 35.54 78.70 72.1072.10 1.86 6.40 4.37 78.70 2.51 12.30 35.54 78.71 72.1072.10 1.86 6.40 4.37 78.71 2.51 12.30 35.54 78.71 72.1072.10 1.86 6.40 4.37 78.71 2.51 12.30 35.55 78.72 72.1172.11 1.86 6.40 4.37 78.72 2.51 12.30 35.55 78.72 72.1172.11 1.86 6.40 4.37 78.72 2.51 12.30 35.55 78.73 72.1172.11 1.86 6.40 4.37 78.73 2.51 12.31 35.55 78.73 72.11

T=72.11°C y P=35.55 kPa

Termodinámica de Ingeniería Química: Equilibrio Vapor Líquido

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Solución Matemática:

ln P1sat=13.8594− 2773.78

t+220.07

ln P2sat=14.0045− 3279.47

t+213.20

P1sat=

y1x1P

P2sat=

y2x2P

ln (α )= 3279.47t+213.20

− 2773.78t+220.07

−0.1451 ; α=P1sat

P2sat=

y1x1y2x2

P=P2sat+ (P1sat−P2sat ) x1

a. x1= 0.35, x2= 0.65, y1=0.70 y y2= 0.30

ln (0.700.350.300.65

)= 3279.47t+213.20

−2773.78t+220.07

−0.1451

1.47= 3279.47t+213.20

− 2773.78t+220.07

−0.1451

t=134.02 °C

ln P1sat=13.8594− 2773.78

134.02+220.07P1sat=413.98kPa

ln P2sat=14.0045− 3279.47

134.02+213.20P2sat=95.54kPa

Termodinámica de Ingeniería Química: Equilibrio Vapor Líquido

Parámetros para la ecuación de AntoineSustancia A B CBenceno 13.8594 2773.78 220.07

Etilenceno 14.0045 3279.47 213.20

Page 10: Termodinamica Para Ingenieria Quimica Ejercicio

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P=P2sat+ (P1sat−P2sat ) x1

P=95.54+(413.98−95.54 )0.35P=206.99 kPa

b. x1= 0.35, x2= 0.65, y1=0.725 y y2= 0.275

ln (0.7250.350.2750.65

)= 3279.47t+213.20

−2773.78t+220.07

−0.1451

1.59= 3279.47t+213.20

− 2773.78t+220.07

−0.1451

t=111.65 °C

ln P1sat=13.8594− 2773.78

111.65+220.07

P1sat=244.13kPa

ln P2sat=14.0045− 3279.47

111.65+213.20

P2sat=49.87kPa

P=P2sat+ (P1sat−P2sat ) x1

P=49.87+(244.13−49.87 )0.35

P=117.86 kPa

c. x1= 0.35, x2= 0.65, y1=0.75 y y2= 0.25

ln (0.750.350.250.65

)= 3279.47t+213.20

−2773.78t+220.07

−0.1451

Termodinámica de Ingeniería Química: Equilibrio Vapor Líquido

Page 11: Termodinamica Para Ingenieria Quimica Ejercicio

10

1.72= 3279.47t+213.20

− 2773.78t+220.07

−0.1451

t=91.15 ° C

ln P1sat=13.8594− 2773.78

91.15+220.07

P1sat=140.74kPa

ln P2sat=14.0045− 3279.47

91.15+213.20

P2sat=25.26kPa

P=P2sat+ (P1sat−P2sat ) x1

P=25.26+(140.74−25.26 )0.35

P=65.68kPa

d. x1= 0.35, x2= 0.65, y1=0.775 y y2= 0.225

ln (0.7750.350.2250.65

)= 3279.47t+213.20

−2773.78t+220.07

−0.1451

1.86= 3279.47t+213.20

− 2773.78t+220.07

−0.1451

t=72.18 °C

ln P1sat=13.8594− 2773.78

72.18+220.07

P1sat=78.90kPa

ln P2sat=14.0045− 3279.47

72.18+213.20

P2sat=12.34kPa

P=P2sat+ (P1sat−P2sat ) x1

Termodinámica de Ingeniería Química: Equilibrio Vapor Líquido

Page 12: Termodinamica Para Ingenieria Quimica Ejercicio

11

P=12.34+(78.90−12.34 )0.35

P=35.64 kPa

Termodinámica de Ingeniería Química: Equilibrio Vapor Líquido