Simulación de proceso de producción de anhídrido ftálico

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1 2 3 4 C-1701 P-1701 E-1701 E-1702 C-1701 P-1701 VAPOR LIQUID VAPOR LIQUID Substream: M Mole Flow km PHTHA-01 0 0 0 0 MALEI-01 0 0 0 0 O-XYL-01 0 0.0256944 0 0.0256944 OXYGE-01 0.7112413 0 0.7112413 0 NITRO-01 2.675622 0 2.675622 0 CARBO-01 0 0 0 0 WATER 0 0 0 0 Total Flow km 3.386863 0.0256944 3.386863 0.0256944 Total Flow kg 97.71236 2.727912 97.71236 2.727912 Total Flow cu 104.9139 3.17E-03 45.04068 3.17E-03 Temperature 298.15 298.15 551.1198 298.2283 Pressure N/s 80000 1.01E+05 3.45E+05 3.45E+05 Vapor Frac 1 0 1 0 Liquid Frac 0 1 0 1 Solid Frac 0 0 0 0 Enthalpy J/k -6455.425 -2.35E+07 7.48E+06 -2.34E+07 Enthalpy J/k -223.7552 -2.21E+05 2.59E+05 -2.21E+05 Enthalpy MM -0.0746018 -2.057466 86.45448 -2.054173 Entropy J/k 6218.911 -4.49E+05 12213.26 -4.49E+05 Entropy J/k 215.5572 -4230.033 423.3306 -4229.795 Density km 0.0322823 8.11047 0.0751956 8.111647 Density kg/ 0.9313577 861.0675 2.169424 861.1925 Average MW 28.8504 106.1674 28.8504 106.1674 Liq Vol 60F cu 0.181393 3.09E-03 0.181393 3.09E-03 *** ALL PHASE CPCVMX 1.400816 1.144743 1.381212 1.144509 Liq Vol 60F cu 0.0535578 0.120264 0.0535578 0.120264 1 2 3 4 C-1701 P-1701 E-1701 E-1702 C-1701 P-1701 VAPOR LIQUID VAPOR LIQUID Substream: M Mole Flow km PHTHA-01 0 0 0 0 MALEI-01 0 0 0 0 O-XYL-01 0 0.0256944 0 0.0256944 OXYGE-01 0.7112413 0 0.7112413 0

description

Comparación de una simulación de procesos

Transcript of Simulación de proceso de producción de anhídrido ftálico

Page 1: Simulación de proceso de producción de anhídrido ftálico

1 2 3 4C-1701 P-1701 E-1701 E-1702

C-1701 P-1701VAPOR LIQUID VAPOR LIQUID

Substream: MIX Mole Flow km PHTHA-01 0 0 0 0 MALEI-01 0 0 0 0 O-XYL-01 0 0.0256944 0 0.0256944 OXYGE-01 0.7112413 0 0.7112413 0 NITRO-01 2.675622 0 2.675622 0 CARBO-01 0 0 0 0 WATER 0 0 0 0Total Flow kmo 3.386863 0.0256944 3.386863 0.0256944Total Flow kg/s 97.71236 2.727912 97.71236 2.727912Total Flow cum 104.9139 3.17E-03 45.04068 3.17E-03Temperature K 298.15 298.15 551.1198 298.2283Pressure N/s 80000 1.01E+05 3.45E+05 3.45E+05Vapor Frac 1 0 1 0Liquid Frac 0 1 0 1Solid Frac 0 0 0 0Enthalpy J/km -6455.425 -2.35E+07 7.48E+06 -2.34E+07Enthalpy J/kg -223.7552 -2.21E+05 2.59E+05 -2.21E+05Enthalpy MM-0.0746018 -2.057466 86.45448 -2.054173Entropy J/k 6218.911 -4.49E+05 12213.26 -4.49E+05Entropy J/kg 215.5572 -4230.033 423.3306 -4229.795Density km 0.0322823 8.11047 0.0751956 8.111647Density kg/ 0.9313577 861.0675 2.169424 861.1925Average MW 28.8504 106.1674 28.8504 106.1674Liq Vol 60F cu 0.181393 3.09E-03 0.181393 3.09E-03*** ALL PHASES CPCVMX 1.400816 1.144743 1.381212 1.144509Liq Vol 60F cu 0.0535578 0.120264 0.0535578 0.120264

1 2 3 4C-1701 P-1701 E-1701 E-1702

C-1701 P-1701VAPOR LIQUID VAPOR LIQUID

Substream: MIX Mole Flow km PHTHA-01 0 0 0 0 MALEI-01 0 0 0 0 O-XYL-01 0 0.0256944 0 0.0256944 OXYGE-01 0.7112413 0 0.7112413 0

Page 2: Simulación de proceso de producción de anhídrido ftálico

NITRO-01 2.675622 0 2.675622 0 CARBO-01 0 0 0 0 WATER 0 0 0 0Total Flow kmo 3.386863 0.0256944 3.386863 0.0256944Total Flow kg/s 97.71236 2.727912 97.71236 2.727912Total Flow cum 104.9139 3.17E-03 45.04068 3.17E-03Temperature K 298.15 298.15 551.1198 298.2283Pressure N/s 80000 1.01E+05 3.45E+05 3.45E+05Vapor Frac 1 0 1 0Liquid Frac 0 1 0 1Solid Frac 0 0 0 0Enthalpy J/km -6455.425 -2.35E+07 7.48E+06 -2.34E+07Enthalpy J/kg -223.7552 -2.21E+05 2.59E+05 -2.21E+05Enthalpy Watt -21863.64 -6.03E+05 2.53E+07 -6.02E+05Entropy J/k 6218.911 -4.49E+05 12213.26 -4.49E+05Entropy J/kg 215.5572 -4230.033 423.3306 -4229.795Density km 0.0322823 8.11047 0.0751956 8.111647Density kg/ 0.9313577 861.0675 2.169424 861.1925Average MW 28.8504 106.1674 28.8504 106.1674Liq Vol 60F cu 0.181393 3.09E-03 0.181393 3.09E-03

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5 6 7 8 9 10M-1701 M-1701 R-1701 E-1703 E-1704 E-1705E-1701 E-1702 M-1701 R-1701 E-1703 E-1704VAPOR VAPOR VAPOR VAPOR VAPOR VAPOR

0 0 0 0.0179861 0.0179861 0.01798610 0 0 2.57E-03 2.57E-03 2.57E-030 0.0256944 0.0256944 0 0 0

0.7112413 0 0.7112413 0.5840538 0.5840538 0.58405382.675622 0 2.675622 2.675622 2.675622 2.675622

0 0 0 0.0513888 0.0513888 0.05138880 0 0 0.0899305 0.0899305 0.0899305

3.386863 0.0256944 3.412558 3.421551 3.421551 3.42155197.71236 2.727912 100.4403 100.4403 100.4403 100.440346.66477 0.3318399 48.56771 81.93345 85.70519 90.07578

513.15 513.15 512.9942 633.15 541.978 443.1713.10E+05 3.10E+05 3.00E+05 2.20E+05 1.80E+05 1.40E+05

1 1 1 1 1 10 0 0 0 0 00 0 0 0 0 0

6.34E+06 5.56E+07 6.71E+06 -4.17E+06 -7.07E+06 -1.01E+072.20E+05 5.24E+05 2.28E+05 -1.42E+05 -2.41E+05 -3.45E+0573.23385 4.875681 78.10953 -48.73063 -82.56734 -118.369110953.07 -2.63E+05 9526.668 20027.56 16756.02 12602.29379.6505 -2479.125 323.678 682.2493 570.8028 429.3036

0.0725785 0.0774302 0.0702639 0.0417601 0.0399223 0.03798522.093921 8.220568 2.068046 1.225876 1.171928 1.115064

28.8504 106.1674 29.43255 29.35519 29.35519 29.355190.181393 3.09E-03 0.1844831 0.1811537 0.1811537 0.1811537

1.385465 1.052384 1.362871 1.349755 1.361456 1.373763

0.0535578 0.120264 0.05406 0.0529449 0.0529449 0.0529449

5 6 7 8 9 10M-1701 M-1701 R-1701 E-1703 E-1704 E-1705E-1701 E-1702 M-1701 R-1701 E-1703 E-1704VAPOR VAPOR VAPOR VAPOR VAPOR VAPOR

0 0 0 0.0179861 0.0179861 0.01798610 0 0 2.57E-03 2.57E-03 2.57E-030 0.0256944 0.0256944 0 0 0

0.7112413 0 0.7112413 0.5840538 0.5840538 0.5840538

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2.675622 0 2.675622 2.675622 2.675622 2.6756220 0 0 0.0513888 0.0513888 0.05138880 0 0 0.0899305 0.0899305 0.0899305

3.386863 0.0256944 3.412558 3.421551 3.421551 3.42155197.71236 2.727912 100.4403 100.4403 100.4403 100.440346.66477 0.3318399 48.56772 81.93345 85.70519 90.07578

513.15 513.15 512.9944 633.15 541.978 443.1713.10E+05 3.10E+05 3.00E+05 2.20E+05 1.80E+05 1.40E+05

1 1 1 1 1 10 0 0 0 0 00 0 0 0 0 0

6.34E+06 5.56E+07 6.71E+06 -4.17E+06 -7.07E+06 -1.01E+072.20E+05 5.24E+05 2.28E+05 -1.42E+05 -2.41E+05 -3.45E+052.15E+07 1.43E+06 2.29E+07 -1.43E+07 -2.42E+07 -3.47E+0710953.07 -2.63E+05 9526.675 20027.56 16756.02 12602.29379.6505 -2479.125 323.6783 682.2493 570.8028 429.3036

0.0725785 0.0774302 0.0702639 0.0417601 0.0399223 0.03798522.093921 8.220568 2.068046 1.225876 1.171928 1.115064

28.8504 106.1674 29.43255 29.35519 29.35519 29.355190.181393 3.09E-03 0.1844831 0.1811537 0.1811537 0.1811537

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11 12 13 14 15SC-1701 B3E-1705 SC-1701 SC-1701 B3 B3MIXED VAPOR LIQUID LIQUID LIQUID

0.0179861 1.80E-04 0.0178062 3.56E-05 0.01777062.57E-03 5.14E-05 2.52E-03 2.51E-03 5.04E-06

0 0 0 0 00.5840538 0.5840538 0 0 0

2.675622 2.675622 0 0 00.0513888 0.0513888 0 0 00.0899305 0.0899305 0 0 0

3.421551 3.401227 0.0203243 2.55E-03 0.0177756100.4403 97.55593 2.884341 0.2516967 2.63264489.89823 89.93473 2.25E-03 1.80E-04 2.06E-03

318.15 318.15 318.15 318.15 318.151.00E+05 1.00E+05 1.00E+05 1.00E+05 1.00E+05

0.9936284 1 0 0 06.37E-03 0 1 1 1

0 0 0 0 0-1.44E+07 -1.18E+07 -4.51E+08 -4.59E+08 -4.51E+08-4.91E+05 -4.11E+05 -3.18E+06 -4.65E+06 -3.04E+06

-168.261 -136.7664 -31.30864 -3.990332 -27.326664099.864 6268.702 -3.51E+05 -2.75E+05 -3.66E+05

139.664 218.5544 -2474.537 -2785.561 -2469.7070.0380602 0.0378188 9.052815 14.13973 8.613763

1.117266 1.084741 1284.738 1396.405 1275.73129.35519 28.68257 141.9159 98.75758 148.1038

0.1811537 0.1789804 2.17E-03 1.84E-04 1.99E-03

1.383685 1.395764 1.135074 1.147183 1.1333940.0529449 0.0526223 0.1069311 0.0721318 0.1119206

11 12 13 14 15SC-1701 T-1701E-1705 SC-1701 SC-1701 T-1701 T-1701MIXED VAPOR LIQUID LIQUID LIQUID

0.0179861 1.80E-04 0.0178062 3.56E-05 0.01777062.57E-03 5.14E-05 2.52E-03 2.51E-03 5.04E-06

0 0 0 0 00.5840538 0.5840538 0 0 0

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2.675622 2.675622 0 0 00.0513888 0.0513888 0 0 00.0899305 0.0899305 0 0 0

3.421551 3.401227 0.0203243 2.55E-03 0.0177756100.4403 97.55593 2.884341 0.2516967 2.63264489.89823 89.93473 2.25E-03 1.80E-04 2.06E-03

318.15 318.15 318.15 318.15 318.151.00E+05 1.00E+05 1.00E+05 1.00E+05 1.00E+05

0.9936284 1 0 0 06.37E-03 0 1 1 1

0 0 0 0 0-1.44E+07 -1.18E+07 -4.51E+08 -4.59E+08 -4.51E+08-4.91E+05 -4.11E+05 -3.18E+06 -4.65E+06 -3.04E+06-4.93E+07 -4.01E+07 -9.18E+06 -1.17E+06 -8.01E+064099.864 6268.702 -3.51E+05 -2.75E+05 -3.66E+05

139.664 218.5544 -2474.537 -2785.561 -2469.7070.0380602 0.0378188 9.052815 14.13973 8.613763

1.117266 1.084741 1284.738 1396.405 1275.73129.35519 28.68257 141.9159 98.75758 148.1038

0.1811537 0.1789804 2.17E-03 1.84E-04 1.99E-03