Question: Repeat the computer simulation proof of feasibility for Example 11-3 but with no recycle. The input for the simulator should be based on the solution

Repeat the computer simulation proof of feasibility for Example 11-3 but with no recycle. The input for the simulator should be based on the solution to Problem 11.D7.
Example 11-3

We have 100.0 kmol/h of a saturated liquid feed that is 50.0

Data From Problem 11.D7

Repeat the residue curve analysis for Example \(11-3\) but with no recycle:

a. For the process in Figure 11-7A.

mol% methanol, 10.0 mol% methyl butyrate, and 40.0 mol% toluene. We want

b. For the process in Figure 11-7B.

to separate this feed into three pure products (99.7+% purities). Develop a

a. For the process in Figure 11-7A.
feasible distillation cascade for this system. Prove that your system is feasible.b. For the process in Figure 11-7B.

image text in transcribed

We have 100.0 kmol/h of a saturated liquid feed that is 50.0 mol% methanol, 10.0 mol% methyl butyrate, and 40.0 mol% toluene. We want to separate this feed into three pure products (99.7+% purities). Develop a feasible distillation cascade for this system. Prove that your system is feasible.

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