Question

In: Chemistry

An air stream is saturated with a vapor (B) at 130F and 1 atm pressure. It...

An air stream is saturated with a vapor (B) at 130F and 1 atm pressure. It is cooled down to 80F where some of the B is condensed and separated from the vapor stream. The remaining vapor stream is then reheated back to 130F.


a. What is the mole fraction of B in the air coming out of the process?

b. For an inlet flow rate of 2000 ft3/min of air saturated with B, what would be the flow rate of the liquid B stream (lb/min)?

c. If the process could cool the stream down to 50F instead of 80F, what would be the outlet mole fraction of B in this case?



Note:
Vapor pressure of B at 80F = 0.5067 psia
Vapor pressure of B at 130F = 2.221 psia MW of B = 20

Heat capacity of liquid B = 0.87 (btu)/(lb)(F)

Solutions

Expert Solution

1 atm =14.7 psia

At 130 deg.F, air stream is saturated. Partial pressure = vapor pressure = 2.221 Psia

Moles of water vapor/ moles of dry air = partial pressure of water vapor/ partial pressure of dry air = 2.221/(14.7-2.221)= 0.1779

Moles of water vapor = 0.1779* moles of dry air

Flow rate = 2000ft3/min Temperature= 130 deg.F = 130+460=590R, P= 14.7 Psia

R= 10.731 psift3

Total number of moles, n= PV/RT= 14.7*2000/(10.731*590) = 4.643 lb moles/min

Moles of water vapor + moles of dry air = 4.643

Molar flow rate of B vapor + moles of B vapor/0.1779= 4.643

Molar flow rate of B vapour (1+1/0.1779)= 4.643

Molar flow rate of B vapour = 4.643/6.621= .7012 lb moles/min = 0.7012*20 lb/min=14.024 lb/min

At exit the air is assumed to be saturated. Hence partial pressure = 0.5067 Psia

Moles of B vapor/ mole of dry air = 0.5067/(14.7-0.5067)= 0.0357

Moles of B vapor = 0.0357* moles of dry air

Moles of B condensed = moles of water vapor at 130deg.F- moles of water vapor at 80 deg.F= Moles of dry air*(0.1779-0.0357)= 0.1422* mole of dry air

Moles of B vapor at 80 deg.F= 0.0357* moles of dry air

Moles of B vapor/ moles of dry air =0.0357

moles of dry air/ mole of B vapor = 1/0.0357 = 28.01

1+ moles of dry air/mole of B vapor =29.01

Moles of wet air/ moles of B vapor = 29.01

Moles of B vapor/ moles of wet air = 1/29.01= 0.0344

Mole fraction of B vapor at 80 deg.F ( outlet)=0.0344

At 50 deg.F, vapor pressure of B need to be calculated. For that deltah/R need to be calculated. This is done by using Classis- Clayperon equation.

Ln(P2/P1)= (deltaH/R)*(1/T1-1/T2)

Ln (2.221/0.5067)= (deltaH/R)*(1/80+460 – 1/130+460)

deltaH/R = 9416.5

at 50 deg.F (T1)= 50+460= 510R

ln(2.221/P1)= 9416.5*(1/510-1/590)

P1= 0.1816 psia

So at 50deg.F, moles of B vapor = 0.1816/(14.7-0.1816)* moles of dry air

Moles of B vapor = 0.01251* moles of dry air

Mole of dry air/ mole of B vapor = 1/0.01251= 79.93

1+ moles of dry air/moles of B vapor = 80.93

Mole of wet air/ moles of B = 80.93

Mole of B/ total moles = 1/80.93= 0.0123

Mole fraction of B at 50 deg.F =0.0123


Related Solutions

500 kmol/h of an air stream at a pressure of 2 atm is to be heated...
500 kmol/h of an air stream at a pressure of 2 atm is to be heated from 15 celsius to 90 celsius in a heat exchanger with 600 kPa steam condensing in the shell side of the heat exchanger. Steam enters the exchanger as a saturated vapor and leaves as a saturated liquid. A) How much steam would be required if a conventional heat exchanger were used? what is the total entropy change during this process? B) How much steam...
Chloroform has a vapor pressure of 197 mmHg at 73.4 F, and 0.5895 atm at 45.0...
Chloroform has a vapor pressure of 197 mmHg at 73.4 F, and 0.5895 atm at 45.0 °C. Estimate its heat of vaporization and normal boiling point.
120 kilograms of saturated water at 2.32 MPa pressure is heated to saturated vapor at same...
120 kilograms of saturated water at 2.32 MPa pressure is heated to saturated vapor at same pressure. Determine heat required for the process.
Air at a pressure of 1 atm and a temperature of 50°C is in parallel flow...
Air at a pressure of 1 atm and a temperature of 50°C is in parallel flow over the top surface of a flat plate that is heated to a uniform temperature of 100°C. The plate has a length of 0.24 m (in the flow direction) and a width of 0.12 m. The Reynolds number based on the plate length is 30,000. (a) What is the rate of heat transfer from the plate to the air? (b) If the free stream...
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...
The capacity of a propane vapor-compression refrigeration system is 8 tons. Saturated vapor at 0°F enters...
The capacity of a propane vapor-compression refrigeration system is 8 tons. Saturated vapor at 0°F enters the compressor, and superheated vapor leaves at 120°F, 180 lbf/in.2 Heat transfer from the compressor to its surroundings occurs at a rate of 3.5 Btu per lb of refrigerant passing through the compressor. Liquid refrigerant enters the expansion valve at 85°F, 180 lbf/in.2 The condenser is water-cooled, with water entering at 65°F and leaving at 80°F with a negligible change in pressure. Determine (a)...
An air-conditioning system operates at a total pressure of 1 atm and consists of a heating...
An air-conditioning system operates at a total pressure of 1 atm and consists of a heating section and an evaporative cooler. Air enters the heating section at 15°C and 55 percent relative humidity at a rate of 30 m3/min, and it leaves the evaporative cooler at 25°C and 45 percent relatively humidity. Using appropriate software, study the effect of total pressure in the range 94 to 100 kPa and plot the results as functions of total pressure. (Please upload your...
Steam is compressed to a saturated vapor state at constant pressure. The steam started at 2...
Steam is compressed to a saturated vapor state at constant pressure. The steam started at 2 MPa and 365 C. What work was required and what was the specific heat transfer? Please show work so I can actually learn!
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...
What is the total vapor pressure in atm of a solution created by combining 2.32 moles...
What is the total vapor pressure in atm of a solution created by combining 2.32 moles of toluene and 6.56 moles of benzene at 350K? At 350K Pvap, toluene = 0.33 atm and Pvap, benzene = 0.95 atm
ADVERTISEMENT
ADVERTISEMENT
ADVERTISEMENT