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500 moles of a tetrahydrofuran (1)/o-xylene (2) containing 49 mol % tetrahydrofuran is distilled in an atmospheric batch still. A final tetrahydrofuran concentration of 2 mol % in the pot desired. Find the amount of distillate collected, the amount of waste left in the pot, and the average concentration of the distillate. Equilibrium data is given below for the binary system. Note: Use an interpolation interval of 0.01. Familibrium data for tatuabudnefunan (1) a rulone (2) binem. im

500 moles of a tetrahydrofuran (1)/o-xylene (2) containing 49 mol % tetrahydrofuran is distilled in an atmospheric batch still. A final tetrahydrofuran concentration of 2 mol % in the pot desired. Find the amount of distillate collected, the amount of waste left in the pot, and the average concentration of the distillate. Equilibrium data is given below for the binary system. Note: Use an interpolation interval of 0.01. Familibrium data for tatuabudnefunan (1) a rulone (2) binem. im

Introduction to Chemical Engineering Thermodynamics
Introduction to Chemical Engineering Thermodynamics
8th Edition
ISBN:9781259696527
Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Publisher:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Chapter1: Introduction
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PROBLEM 1 500 moles of a tetrahydrofuran (1) / o-xylene (2) containing 49 mol% tetrahydrofuran is distilled in an atmospheric batch still. A final tetrahydrofuran concentration of 2 mol % in the pot desired. Find the amount of distillate collected, the amount of waste left in the pot, and the average concentration of the distillate. Equilibrium data is given below for the binary system. Note: Use an interpolation interval of 0.01. Equilibrium data for tetrahydrofuran (1) / o-xylene (2) binary system: 117.809000 0.150000 0.596974 111.816000 0.200000 0.685587 106.631000 0.250000 0.750857 102.067000 0.300000 0.800432 97.989100 0.350000 0.839049 94.299300 0.400000 0.869757 90.924000 0.450000 0.894593 87.807500 0.500000 0.914952 84.907300 0.550000 0.931819 82.191400 0.600000 0.945899 79.635900 0.650000 0.957710 77.223800 0.700000 0.967636 74.944000 0.750000 0.975967 72.791500 0.800000 0.982926 70.767100 0.850000 0.988684 T X1 yı 143.924000 0.000000 0.000000 143.705000 0.001000 0.007234 143.471000 0.002000 0.014395 143.237000 0.003000 0.021483 143.005000 0.004000 0.028501 142.544000 0.006000 0.042325 142.087000 0.008000 0.055875 141.634000 0.010000 0.069157 139.433000 0.020000 0.131788 137.331000 0.030000 0.188670 135.320000 0.040000 0.240469 131.551000 0.060000 0.331056 128.081000 0.080000 0.407308 124.874000 0.100000 0.472078 68.878100 0.900000 0.993378 68.163500 0.920000 0.994983 67.474100 0.940000 0.996442 66.811500 0.960000 0.997760 66.490900 0.970000 0.998369 66.177700 0.980000 0.998945 65.872200 0.990000 0.999488 65.812000 0.992000 0.999593 65.752200 0.994000 0.999697 65.692700 0.996000 0.999799 65.663100 0.997000 0.999850 65.633500 0.998000 0.999900 65.604100 0.999000 0.999950 65.550600 1.000000 1.000000
Transcribed Image Text:PROBLEM 1 500 moles of a tetrahydrofuran (1) / o-xylene (2) containing 49 mol% tetrahydrofuran is distilled in an atmospheric batch still. A final tetrahydrofuran concentration of 2 mol % in the pot desired. Find the amount of distillate collected, the amount of waste left in the pot, and the average concentration of the distillate. Equilibrium data is given below for the binary system. Note: Use an interpolation interval of 0.01. Equilibrium data for tetrahydrofuran (1) / o-xylene (2) binary system: 117.809000 0.150000 0.596974 111.816000 0.200000 0.685587 106.631000 0.250000 0.750857 102.067000 0.300000 0.800432 97.989100 0.350000 0.839049 94.299300 0.400000 0.869757 90.924000 0.450000 0.894593 87.807500 0.500000 0.914952 84.907300 0.550000 0.931819 82.191400 0.600000 0.945899 79.635900 0.650000 0.957710 77.223800 0.700000 0.967636 74.944000 0.750000 0.975967 72.791500 0.800000 0.982926 70.767100 0.850000 0.988684 T X1 yı 143.924000 0.000000 0.000000 143.705000 0.001000 0.007234 143.471000 0.002000 0.014395 143.237000 0.003000 0.021483 143.005000 0.004000 0.028501 142.544000 0.006000 0.042325 142.087000 0.008000 0.055875 141.634000 0.010000 0.069157 139.433000 0.020000 0.131788 137.331000 0.030000 0.188670 135.320000 0.040000 0.240469 131.551000 0.060000 0.331056 128.081000 0.080000 0.407308 124.874000 0.100000 0.472078 68.878100 0.900000 0.993378 68.163500 0.920000 0.994983 67.474100 0.940000 0.996442 66.811500 0.960000 0.997760 66.490900 0.970000 0.998369 66.177700 0.980000 0.998945 65.872200 0.990000 0.999488 65.812000 0.992000 0.999593 65.752200 0.994000 0.999697 65.692700 0.996000 0.999799 65.663100 0.997000 0.999850 65.633500 0.998000 0.999900 65.604100 0.999000 0.999950 65.550600 1.000000 1.000000
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