Question

A distillation column with a total condenser is separating acetone from ethanol. A distillate concentration of...

A distillation column with a total condenser is separating acetone from ethanol. A distillate concentration of xD = 0.90 mole fraction acetone is desired. Since CMO is valid, L/V = constant. If L/V is equal to 0.8. The distillation column has a partial reboiler that acts as an equilibrium contact. If the bottoms composition is xB = 0.13 mole fraction acetone and the boilup ratio V/B= 1.0, find the vapor composition leaving the second stage above the partial reboiler.

a) Get the Equilibrium data for acetone and ethanol at 1 atm from any suitable reference.

b) Find the composition of the liquid leaving the fifth stage below the total condenser.

c) The distillation column in parts a and b is separating acetone from ethanol and has xD= 0.9, xB= 0.13, L/V= 0.8, and V/B= 1.0. If the feed composition is z = 0.3 (all concentrations are mole fraction of more volatile component), find the optimum feed plate location, total number of stages, and required q value of the feed.

d) How many stages are required at total reflux?

e) What is (L /V)min? What is (L /D)min?

Homework Answers

Know the answer?
Your Answer:

Post as a guest

Your Name:

What's your source?

Earn Coins

Coins can be redeemed for fabulous gifts.

Not the answer you're looking for?
Ask your own homework help question
Similar Questions
Separation of Acetone and Ethanol A distillation column with a total condenser and partial reboiler is...
Separation of Acetone and Ethanol A distillation column with a total condenser and partial reboiler is separating acetone and ethanol (equilibrium data is provided in the table below). The feed is 70 mole% acetone, flows at 1000 mol/h, and is a superheated vapor for which one mole of liquid must be vaporized on the feed plate to cool four moles of feed. We desire a bottoms composition of 5 mole% acetone and a distillate composition of 90 mole% acetone. The...
A continuous, steady-state distillation column with a total condenser and a partial reboiler is separating methanol...
A continuous, steady-state distillation column with a total condenser and a partial reboiler is separating methanol from water at one atmosphere. The feed rate is 100 kg mole per hour. The feed is 55 mole % methanol and 45 mole % water. We desire a distillate product that is 90 mole % methanol and a bottoms product that is 5 mole % methanol. Assume CMO. a- Obtain and use the vapor liquid equilibrium data for methanol –water form any available...
We wish to separate a mixture of 60 mol% ethanol and 40 mol% n-propanol in a...
We wish to separate a mixture of 60 mol% ethanol and 40 mol% n-propanol in a distillation column with a partial reboiler and a total condenser. The feed rate is 1000 kmol/h, and feed is a saturated vapour. We desire a distillate product of 99 mol% ethanol and a bottoms product that is 0.8 mol% ethanol. Reflux is saturated liquid and CMO can be used. Equilibrium data can be approximated with an average relative volatility of 2.1 (ethanol is more...
We have designed a special column that acts as exactly three equilibrium stages. Operating at total...
We have designed a special column that acts as exactly three equilibrium stages. Operating at total reflux, we measure vapor composition leaving the top stage and the liquid composition leaving the bottom stage. The column is separating phenol from o-cresol. We measure a phenol liquid mole fraction leaving the bottom stage of 0.36 and a phenol vapor mole fraction leaving the top stage of 0.545. What is the relative volatility of phenol with respect to o-cresol?
Consider the distillation of a saturated liquid feed of 0.16 mol fraction methanol and 0.84 mol...
Consider the distillation of a saturated liquid feed of 0.16 mol fraction methanol and 0.84 mol fraction water. The column has a side stream of composition 0.5 mol fraction methanol and a flow rate of 7.7% of the feed rate. The top product is to contain 0.77 mol fraction methanol and the bottom product is to contain 0.02 mol fraction methanol. The column operates at 1 atm, and the usual simplifying assumptions can be made. The external reflux ratio is...
11. Your company has a distillation column ready to install. The column has one feed, a...
11. Your company has a distillation column ready to install. The column has one feed, a partial condenser and a partial reboiler. Vapor product is drawn directly from the condenser. Find the number of degrees of freedom with this column. HINT there is no stream divider after the condenser. 12. Using a total condenser with a reflux ratio of 2, the heat load on the condenser is (a) Twice the heat of vaporization of the distillate. (b) Equal to the...