A distillation column is separating a feed that is 40 mol% methanol and 60% water. The two phase feed is 60% liquid. Distillate product should be 92% methanol and bottoms 4 mol%. A total reboiler and a total condenser are used and reflux is saturated. Operation is at atmospheric pressure with a reflux ratio of 0.9. Under these conditions, HG = 1.3 ft and HL = 0.8ft in both the stripping and enriching sections. Determine the required packing height in the enriching section.
The minimum number of stages is seen to be 6. The value is independent of the feed condition because at total reflux, there is no no feed. The temperature of the bottoms is 93.5oC. The temperature of the distillate is 64.7oC
One hundred lbmol/h of a mixture of 69 mol% methanol in water at 30oC and 1 atm is to be separated by distillation at the same pressure into a liquid distillate containing 98 mol% methanol and a bottoms liquid product containing 96 mol% water. The enthalpy of the feed mixture is 765 Btu/lbmol. Determine the minimum number of equilibrium stages, the temperatures of the distillate and the bottoms.
A distillation column is separating a feed that is 40 mol% methanol and 60% water. The...
thats all information i got (b) A saturated vapour of methanol and water contains 45 mol% methanol and is to be separated using an enriching column. 250 kmol/h is fed to the bottom of the column operating at atmospheric pressure. Vapour from the top of the column is to contain 85 mol% methanol. A total condenser operates at the top of the column with a reflux ratio of 1.5 If CMO applies, determine the bottoms composition, the internal flow rates...
A liquid stream, F, containing A and B is fed to a distillation column. The total feed flow is 1000 moles Tray efficiency for the column is 0.65 Reflux is to be operated at 1.7 x Rmin Given: • Mole fraction of A in the feed is 0.45 ; A is the more volatile component • 4-0.75 mole fraction of the feed remaining liquid • The distillate is to contain 0.9 of A; The bottoms is to contain 0.08 of...
A liquid stream, F, containing A and B is fed to a distillation column. The total feed flow is 850 moles Tray efficiency for the column is 0.65 Reflux is to be operated at 2.5 x Rmin Given: • Mole fraction of A in the feed is 0.45; A is the more volatile component . q = 0.8 mole fraction of the feed remaining liquid The distillate is to contain 0.89 of A; The bottoms is to contain 0.07 of...
3. Given the equilibrium data for acetone from ethanol at 1 atm below, 0.262 0.15 0.348 0.417 0.25 0.478 0.524 0.35 0.566 0.605 0.674 0.739 0.802 0.865 0.929 0.1 0.3 0.6 0.7 0.9 Answer the following: A distillation column with a total condenser is separating acetone from ethanol. A distillate concentration of 90 mo1% acetone is desired. Since CMO is valid, LN is constant at 0.80, find the composition of the liquid leaving the 5th stage below the condenser a....
We are separating acetone and ethanol in a distillation column with a total condenser and a partial reboiler. The column has two feeds and operates at a pressure of 1.0 atm. Feed 1 is a saturated liquid that is 60.0 mol% acetone and has a feed rate of F1 = 200.0 kmol/h. The second feed is 40.0 mol% acetone, has a feed rate of F2 = 300.0 kmol/h, and is a two-phase mixture that is 20% vapor. Assume CMO is...
Question 3 A saturated liquid mixture is fed to a continuous distillation column at 300 kmol/h. The specifications of the operation of the column are provided in Table 2. The column operates at 800 kPa. Table 2: Feed, distillate and bottoms flowrates Component Feed (kmol/h) Bottoms (kmol/h) Distillate (kmol/h) methanol 95 ethanol 33 n-propanol (LK) 67 n-butanol (HK) 45 4 n-pentanol 60 Total 300 Additional information: a. n-propanol is the light key component (LK) and n-butanol is the heavy key...
A saturated liquid feed with a composition of 45 mole-% benzene and 55 mole-% toluene is distilled in a plate column at the rate of 250 kmol/h. Overhead product contains 97 mole-% benzene and the bottom product contains 5 mole-% benzene. A total condenser and a partial reboiler are used. The reflux ratio employed is 1.5 times the minimum, RD 1.5 RDmin Find the number of theoretical plates required for this separation, the heat duties of the condenser and reboiler....
2. (no calculations required) A mixture of n-butanol and water is being separated using two distillation columns coupled together by a liquid-liquid separator. Both columns have 30 trays and operate at 1 atm with the internal reflux ratio adjusted to four times the minimum Vapor-liquid- liquid equilibrium data for this system at 1 atm is provided below in the form of a T-x-y diagram. If the feed to the distillation towers is a saturated liquid that contains 65 mol% water,...
Q3 An equimolar binary liquid solution of benzene and toluene is to be separated by rectification in a plate column at atmospheric pressure. The feed is 60 mol percent vapor 40 mole percent liquid and flow rate of feed is 300 kmol/h. It is suggested to operate the column at a reflux ratio 1.7 times its minimum value. The top product should contain 95% benzene and 4 % of the benzene in the feed is loss in to the bottom...
Consider the phase diagram below for a mixture of chloroform and methanol, looking at how the boiling point changes with composition at constant pressure. If you started with a solution that was Xchloroform = 0.1 at a temperature of 333 K, is it possible to use fractional distillation to purify this solution to nearly 100% chloroform? Approximately what concentration (in mole fraction) would you expect you could achieve through fractional distillation? Curves calculated by mod. UNIFAC (Dortmund) Temperature Minimum Azeotrope...