ASPEN

Pls. Solve this as soon as possible

Exercise 2. A total of F kg-mol per hour of a G mol% methanol and H mol% water mixture is to be separated at 1 atm to give a distillate that contains 92 mol% methanol and a bottom product that contains 4 mol% methanol. A total condenser is to be used and the reflux will be returned to the column as a saturated liquid at its bubble point. An operating reflux ratio of 1.5 times the minimum will be used. The feed is introduced into the column as a saturated liquid at its bubble point. Use Aspen Plus to complete the following: a. determine the minimum number of theoretical stages. b. determine the minimum reflux ratio, c. determine the heat loads of the condenser and reboiler for the condition of minimum reflux, d. determine the quantities of the distillate and bottom streams using the actual reflux ratio, e determine the actual number of theoretical stages, f. determine the heat load of the condenser for the actual reflux ratio, . B C D F G H 0.07 0.20 0.25 0.43 0.08 0.35 0.42 GOO 0.15 300 250 25 85 30 70 ni a Exercise 2. A total of F kg-mol per hour of a G mol% methanol and H mol% water mixture is to be separated at 1 atm to give a distillate that contains 92 mol% methanol and a bottom product that contains 4 mol% methanol. A total condenser is to be used and the reflux will be returned to the column as a saturated liquid at its bubble point. An operating reflux ratio of 1.5 times the minimum will be used. The feed is introduced into the column as a saturated liquid at its bubble point. Use Aspen Plus to complete the following: a. determine the minimum number of theoretical stages, b. determine the minimum reflux ratio, c. determine the heat loads of the condenser and reboiler for the condition of minimum reflux, d. determine the quantities of the distillate and bottom streams using the actual reflux ratio, determine the actual number of theoretical stages, f. determine the heat load of the condenser for the actual reflux ratio, e. Exercise 2. A total of F kg-mol per hour of a G mol% methanol and H mol% water mixture is to be separated at 1 atm to give a distillate that contains 92 mol% methanol and a bottom product that contains 4 mol% methanol. A total condenser is to be used and the reflux will be returned to the column as a saturated liquid at its bubble point. An operating reflux ratio of 1.5 times the minimum will be used. The feed is introduced into the column as a saturated liquid at its bubble point. Use Aspen Plus to complete the following: a. determine the minimum number of theoretical stages. b. determine the minimum reflux ratio, c. determine the heat loads of the condenser and reboiler for the condition of minimum reflux, d. determine the quantities of the distillate and bottom streams using the actual reflux ratio, e determine the actual number of theoretical stages, f. determine the heat load of the condenser for the actual reflux ratio, . B C D F G H 0.07 0.20 0.25 0.43 0.08 0.35 0.42 GOO 0.15 300 250 25 85 30 70 ni a Exercise 2. A total of F kg-mol per hour of a G mol% methanol and H mol% water mixture is to be separated at 1 atm to give a distillate that contains 92 mol% methanol and a bottom product that contains 4 mol% methanol. A total condenser is to be used and the reflux will be returned to the column as a saturated liquid at its bubble point. An operating reflux ratio of 1.5 times the minimum will be used. The feed is introduced into the column as a saturated liquid at its bubble point. Use Aspen Plus to complete the following: a. determine the minimum number of theoretical stages, b. determine the minimum reflux ratio, c. determine the heat loads of the condenser and reboiler for the condition of minimum reflux, d. determine the quantities of the distillate and bottom streams using the actual reflux ratio, determine the actual number of theoretical stages, f. determine the heat load of the condenser for the actual reflux ratio, e