Question

In: Other

A distillation column with a partial reboiler and a total condenser is being used to separate...

A distillation column with a partial reboiler and a total condenser is being used to separate a mixture of benzene, toluene, and cumene. The feed is 40 mol% benzene, 30 mol% toluene and 30 mol% cumene. The feed is input as a saturated vapor. We desire 99% recovery of the toluene in the bottoms and 98% recovery of the benzene in the distillate. The reflux is returned as a saturated liquid, and CMO can be assumed. Equilibrium can be represented as constant relative volatilities. Choosing toluene as the reference component, ?benzene-toluene = 2.25 and ?cumene-toluene = 0.210. Use the Fenske equation to find the number of equilibrium stages required at total reflux and the recovery fraction of cumene in the bottoms. b. For the distillation problem given in part a, find the minimum reflux ratio by use of the Underwood equations. Use a basis of 100 moles of feed/h. Clearly state your assumptions. d. For L/D = 1.25(L/D)min , find the total number of equilibrium stages required for the distillation problem presented in parts a and b. Use the Gilliland correlation. Estimate the optimum feed plate location.

Solutions

Expert Solution


Related Solutions

A distillation column with a total condenser and a partial reboiler is separating ethanol and water...
A distillation column with a total condenser and a partial reboiler is separating ethanol and water at 1 kg/cm2 pressure. Feed is 32.0 mol% ethanol and is at 30°C. Feed flow rate is 100.0 kmol/h. The distillate product is a saturated liquid, and distillate is 80.0 mol% ethanol. The condenser removes 2,065,113 kcal/h. The bottoms is 4.0 mol% ethanol. Assume that CMO is valid. Find the number of stages and the optimum feed stage location. Data: CPL,EtOH = 24.65 cal/(mol°C)...
A (LK) equivalent to A (LK) through a distillation column connected to the total condenser and...
A (LK) equivalent to A (LK) through a distillation column connected to the total condenser and partial reboiler. The mixture of substance) and B is to be separated. saturized-liquid feed(F; 100) containing 50 mol% of A When mol/h) is supplied and driven through the design conditions below, the composition of A in the desillate(D) is 0.96. In Bottom(B), the creation of A was 0.18. (a) the total unit of equilibrium (including partial reboiler) and (b) the supply of raw materials;...
Explain the start-up issues in a distillation column. Also, explain the function of reboiler and give...
Explain the start-up issues in a distillation column. Also, explain the function of reboiler and give its types.
Question 2: A train of two distillation colum ns is being used to separate a mixture...
Question 2: A train of two distillation colum ns is being used to separate a mixture of hexane, heptane and octane. The feed to the first column contains 40 mole% hexane, 30 mole% heptane and 30 mole% octane and enters at a rate of 2500 kmol/h. In the first column 98% of the octane fed is recovered in the bottom product. Essentially no hexane goes with the bottom product and the mole fraction of octaine in the bottom is 99.5%....
1. Distillation is used to separate hydrocarbons. What property is used to obtain the separation?
1. Distillation is used to separate hydrocarbons. What property is used to obtain the separation?
If you used the simple distillation to separate cyclohexane and toluene, will it work? Why or...
If you used the simple distillation to separate cyclohexane and toluene, will it work? Why or Why not?
Show all working and formulas used whether with excel or on paper A distillation column is...
Show all working and formulas used whether with excel or on paper A distillation column is designed, purchased and installed for a cost of $1.2 million. The equipment has a depreciable life of ten (10) years with a final salvage value of $50,000 in year 10. For this equipment determine … a. The book value and depreciation allowance for each year using straight-line (SLN) depreciation. b. Book values and depreciation allowances for each year using double-declining (DDB) depreciation.
1. Explain the effects of distillation rate, column packing, and column height on fractionation. When is...
1. Explain the effects of distillation rate, column packing, and column height on fractionation. When is a fractionating column not necessary? (3 points) minimum of 150 words.
Explain how column chromatography can be used to separate a mixture on a larger scale than...
Explain how column chromatography can be used to separate a mixture on a larger scale than TLC?
Multicomponent Distillation 1 A distillation column is separating ethane, propane, and n-butane at 5 atm. Operation...
Multicomponent Distillation 1 A distillation column is separating ethane, propane, and n-butane at 5 atm. Operation is at total reflux. We want a 98.9% recovery of ethane in the distillate and a 99.8% recovery of n-butane in the bottoms. Propane is a sandwich component (e.g., in between light and heavy keys). The feed is a saturated liquid at 100 kmol/h composed of 30.0 mol% ethane, 33.0 mol% propane and 37.0 mol% n-butane. You may assume relative volatilities are constant, αEB...
ADVERTISEMENT
ADVERTISEMENT
ADVERTISEMENT