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) at 0°C. The enthalpy-composition diagram is given in Figure 2-4, and the y-x diagram is in Figure 2-2.

Expert Solution

Amanda K answered 9 months ago

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...

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;...

A distillation column is separating 100 kmol/h of saturated vapor feed that is 30 mol% ethanol,...

A distillation column is separating 100 kmol/h of saturated vapor feed that is 30 mol% ethanol, 25 mol% i-propanol, 35 mol% n-propanol, and 10 mol% n-butanol at a pressure of 1.0 atm. We want a 98.6% recovery of i-propanol in the distillate and 99.2% recovery of n-propanol in the bottoms. The column has a total condenser and a partial reboiler. The distillate flow rate in kmol/hr is ___________, the bottoms flow rate in kmol/hr is ____________, the molar fraction of i-propanol in...

After fermentation, a mixture of ethanol and water is sent to a small distillation column. At...

After fermentation, a mixture of ethanol and water is sent to a small distillation column. At the top of the distillation column, a 95% ethanol solution at 65°C is produced at a flow rate of 3.5 kg/s. Your job is to design a double-pipe heat exchanger that will cool the 95% ethanol mixture to 40°C by using cooling water that is available at 10°C. Assume an outlet temperature of the cooling water of 55°C, and only use Schedule 40 pipe...

The ethanol-water mixture is separated on a distillation column. Feed contains 20% ethanol and 1000 kmol...

The ethanol-water mixture is separated on a distillation column. Feed contains 20% ethanol and 1000 kmol / hour speed is entering the system. The feed temperature is 30ºC and its enthalpy is 15kcal / kg. Saturated feed steam enthalpy 485 kcal / kg and saturated feed liquid enthalpy 70kcal / kg. Distillate has at least 80% ethanol and 2% ethanol concentration of the sub-product is required to be. The feedback / distillate ratio is 5/3. System pressure is 1 atm....

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.

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...

 Briefly explain the process of fractional distillation – the physical process for separating gasoline and...

 Briefly explain the process of fractional distillation – the physical process for separating gasoline and kerosene (the two types of aviation fuels) from crude oil.  Differentiate between a physical property and a chemical property of a substance.  Regarding the organic chemical compounds which are the primary component of jet fuel, hydrocarbons - Describe the types of chemical bonds occurring between carbon atoms. - Describe the shapes formed by single-bonded hydrocarbon chains. - Explain how the electron configuration...

Distillation is a process for separating and collecting substances according to their reaction to heat. When...

Distillation is a process for separating and collecting substances according to their reaction to heat. When heat is applied to a mixture, the substance that evaporates and is collected as it cools is the distillate. The unevaporated portion of the mixture is the residue. Oil obtained from orange blossoms through distillation is used in perfume. Suppose the oil yield is normally distributed. In a random sample of eleven distillations, the sample mean oil yield was 980.2 grams with sample standard...

Water enters the condenser of surface type; the temperatures of the water that is used to...

Water enters the condenser of surface type; the temperatures of the water that is used to cool the steam is 17oC and 28oC respectively. The pressure of the condenser is at 0.055 bar and 0.87 dry fraction. The overall heat transfer coefficient in the condenser is 3 kW/m2.oC. The condenser has three passes and tubes used have 17.6 mm internal diameter and 20 mm external diameter. If the flow area is 1.3 m2, Design the condenser. If the condenser is...

Question