Fill in the rows for (mathrm{x}_{mathrm{L}}=0.25) and 0.4 in Table 8-3. TABLE 8-3. Results for two-stage cross-flow

Fill in the rows for \(\mathrm{x}_{\mathrm{L}}=0.25\) and 0.4 in Table 8-3.

Transcribed Image Text:

TABLE 8-3. Results for two-stage cross-flow steam distillation system shown in Figure 8-7A XL L kmol/h n org 1 nw1 norg2 nw2 nw total VPC10 0.15 5.882 4.118 296.6 0 0 301.22 68.0 0.2 6.25 3.75 202.3 0.368 26.49 233.35 67.8 0.25 - 0.29 7.042 2.958 109.7 1.16 83.56 197.86 67.4 0.294 7.082 2.918 106.7 1.20 86.43 197.77 67.42 * 0.295 7.092 2.908 106.0 1.21 87.156 197.76 67.42 * 0.296 7.102 2.898 105.3 1.22 87.88 197.76 67.42 * 0.297* 7.112 2.888 104.6 1.23 88.61 197.76 67.41 0.3 7.143 2.857 102.4 1.26 90.81 197.81 67.40 0.35 7.692 2.308 70.79 1.81 130.39 205.77 67.2 0.4 - 0.45 9.091 0.909 21.62 3.21 231.14 257.35 66.8 0.5 10 0 0 4.118 296.63 301.22 66.6 Runs with lowest value of nw,total including the steam required for evaporating organic liquid.