Results of design calculations for a methanol-water distillation operation are given in Figure 7.50. (a) Calculate the

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Results of design calculations for a methanol-water distillation operation are given in Figure 7.50.

(a) Calculate the column diameter at the top tray and at the bottom tray for sieve trays. Should the column be swaged?

(b) Calculate the length and diameter of' the horizontal refluxdrum

Saturated liquid 189°F 33 psia 32 462,385 Ib/h 99.05 mole % methanol Feed 442,900,000 Btu/h 262.5°F, 40 psia 188,975 I

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Separation process principles

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Question Posted: Jul 25, 2011 07:38 AM

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Results of design calculations for a methanol-water distillation operation are given in Figure 7.50. (a) Calculate the

Question:

Saturated liquid 189°F 33 psia 32 462,385 Ib/h 99.05 mole % methanol Feed 442,900,000 Btu/h 262.5°F, 40 psia 188,975 Ib/h 1.01 mol% methanol Figure 7.50 Data for Exercise 7.47.

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First compute the liquid and vapor flow rates at the top and bottom of the column Molecular weight of distillate 099053204 000951802 3191 Distillate f...View the full answer

Separation process principles

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