Question

In: Other

The vapor-liquid equilibrium data for heptane – ethylbenzene at 1 atm pressure is given below: x...

The vapor-liquid equilibrium data for heptane – ethylbenzene at 1 atm pressure is given below:

x

0

0.10

0.20

0.40

0.50

0.60

0.70

0.90

1

y

0

0.25

0.45

0.65

0.74

0.82

0.86

0.96

1

            A feed mixture containing 40 mol% heptane and 60 mol% ethylbenzene is to be fractionated at 1 atm pressure to produce a distillate containing 95 mol% heptane and a bottom product stream containing 96 mol% ethylbenzene.

Determine the minimum reflux ratio if the feed is a saturated liquid.

Determine the minimum reflux ratio if the feed is a saturated vapor.

Determine the minimum reflux ratio if the feed is an equilibrium mixture of liquid and vapor, with 20% vapor.

Determine the minimum number of theoretical plates using McCabe-Thiele graphical method.

Determine the minimum number of theoretical plates using Fenske equation.

For a saturated liquid feed and a reflux ratio that is 2.25 times the minimum, determine:

-The number of theoretical stages, using McCabe-Thiele graphical method.

-The optimum feed stage location.

-The actual number of stages if the average column efficiency is 58%.

-The top product and bottom product rates if the feed rate is 100 kmol/s.

-The condenser duty.

-The reboiler duty.

Latent heat, kJ/kmol

Heat capacity, kJ/kmol-K

Heptane

35,000

220

Ethylbenzene

40,000

183

Feed temperature

30C

Condenser temperature

95C

Reboiler temperature

99C

                                                                          

Solutions

Expert Solution

Draw the equilibrium diagram from the given x and y values.

Feed is 40 mol% heptane and 60 mol% ethylbenzene.

Distillate from the distillation column consists of 95 mol% heptane and bottoms from the distillaiton column consists of 96 mol% ethylbenzene.

Therefore,

Here shows mole fraction of more volatile component. i.e heptane.

(a)  Determine the minimum reflux ratio if the feed is a saturated liquid.

If feed is saturated liquid,

Slope of feed line is infinity. i.e feed line vertical line from the feed location.

At minimum reflux ratio all rectifying section operating line, stipping section operating line, and feed line will intersect on equilibrium curve.

(b) Determine the minimum reflux ratio if the feed is a saturated vapor.

(c) Determine the minimum reflux ratio if the feed is an equilibrium mixture of liquid and vapor, with 20% vapor.

is the fraction of liquid in feed.

(d) Minimum number of plares required for given separaion at total reflux ratio. at this condition both rectifying section and stripping section operating lines will coinside with diagonal line.


Related Solutions

Given: Vapor–liquid equilibrium data in mole fractions for the system acetone–air–water at 1 atm (101.3 kPa)...
Given: Vapor–liquid equilibrium data in mole fractions for the system acetone–air–water at 1 atm (101.3 kPa) are as follows: y acetone in air 0.004 0.008 0.014 0.017 0.019 0.020 x acetone in water 0.002 0.004 0.006 0.008 0.010 0.012 Find: (a) Plot the data as (1) moles acetone per mole air versus moles acetone per mole water, (2) partial pressure of acetone versus g acetone per g water, and (3) y versus x. (b) If 20 moles of gas containing...
Calculate the normal boiling point of liquid Q if the vapor pressure is .500 atm at...
Calculate the normal boiling point of liquid Q if the vapor pressure is .500 atm at 20 degrees C. The change/ delta of H of vaporization for liquid Q is 26 kJ/ mole. Do you except liquid Q to have H bonds?
The equilibrium vapor pressure of ethanol at 298.15 K is 0.078 atm. Will ethanol gas at...
The equilibrium vapor pressure of ethanol at 298.15 K is 0.078 atm. Will ethanol gas at 0.05 atm and 298.15 K spontaneously condense to liquid ehtanol? First answer this by thinking about it qualitatively. Then support it with a calculation. Use the change in entropy of the system and calculate the change in entropy of the surroundings, and the change in entropy of the universe for the condensation of one mole of ethanol gas at 0.05 atm and 298.15 K...
Vapor pressure data are given here for 1-nitropropane, . Temperature (°C) Vapor Pressure (mm Hg) 25...
Vapor pressure data are given here for 1-nitropropane, . Temperature (°C) Vapor Pressure (mm Hg) 25 21.0 50. 66.2 75 177.1 100. 415.1 Use the Clausius–Clapeyron equation to calculate the molar enthalpy of vaporization of 1-nitropropane and its normal boiling point. Molar enthalpy = ? kJ/mol Normal boiling point = ? K
18. Explain why the vapor pressure of water in equilibrium with liquid water is temperature dependent?
18. Explain why the vapor pressure of water in equilibrium with liquid water is temperature dependent?
The equilibrium vapor pressure of mercury at room temperature is about 1.6x10-6 atm. Imagine an old...
The equilibrium vapor pressure of mercury at room temperature is about 1.6x10-6 atm. Imagine an old chemistry lab that over the years has experienced enough liquid mercury spills and thereby accumulated enough mercury in cracks in the floor, etc. that mercury liquid-vapor equilibrium has been established. What is the concentration, in the units of milligrams per cubic meter, of Hg0 in the air of the room? Does this value exceed the limit of 0.05 mg m-3 established by the American...
Data for benzene and toluene are given below. Calculate the vapor pressure over a solution made...
Data for benzene and toluene are given below. Calculate the vapor pressure over a solution made by mixing 20.0 grams of benzene with 80.0 grams of toluene when the temperature is 40.0ºC. Compound      Molar Mass                 Vapor Pressure at 40.0ºC Benzene          78.11 g/mol                 183 mm Hg Toluene           92.14 g/mol                 59 mm Hg
Some vapor pressure data for ethanol/water are given below. From this data, determine the Henry’s Law...
Some vapor pressure data for ethanol/water are given below. From this data, determine the Henry’s Law constant for each substance. XEthanol PEthanol (/torr) PWater (/torr) 0.00 0.00 23.78 0.02 4.28 23.31 0.05 9.96 22.67 0.08 14.84 22.07 0.10 17.65 21.70 0.20 27.02 20.25 0.30 31.23 19.34 0.40 33.93 18.50 0.50 36.86 17.29 0.60 40.23 15.53 0.70 43.94 13.16 0.80 48.24 9.89 0.90 53.45 5.38 0.93 55.14 3.83 0.96 56.87 2.23 0.98 58.02 1.13 1.00 59.20 0.00 Estimate, based on your...
The vapor pressure, P, of a certain liquid was measured at two temperatures, T. The data...
The vapor pressure, P, of a certain liquid was measured at two temperatures, T. The data is shown in this table.    T(K) P(kPa) 325 3.54 675 8.12 If you were going to graphically determine the enthalpy of vaporizaton, ΔHvap, for this liquid, what points would you plot?
At a certain temperature the vapor pressure of pure heptane C7H16 is measured to be 454.mmHg...
At a certain temperature the vapor pressure of pure heptane C7H16 is measured to be 454.mmHg . Suppose a solution is prepared by mixing 102.g of heptane and 135.g of chloroform CHCl3 . Calculate the partial pressure of heptane vapor above this solution. Be sure your answer has the correct number of significant digits. Note for advanced students: you may assume the solution is ideal.
ADVERTISEMENT
ADVERTISEMENT
ADVERTISEMENT