Question

A mixture, F, of 620 lbmol/h of 46 mol% benzene (B) and 54 mol% toluene (T)...

A mixture, F, of 620 lbmol/h of 46 mol% benzene (B) and 54 mol% toluene (T) is separated continuously into two products. One product, the distillate , is 98 mol% benzene. The other product, the bottoms , is 95 mol% toluene. Compute the flow rates of these two streams in: (a) lbmol/h, and (b) kmol/h. Calculate the fraction of the benzene fed to the unit that is recovered in the distillate.

Homework Answers

Answer #1

F = 620

xb = 0.46

xt = 0.54

P = ?

xb = 0.98

xt = 0.02

B = ?

xb= 0.95

xt = 0.05

Calculate

A) B and P (lbmol/h and kmol/h)

F = B + P

620 = B + P

balance Toluene

620*0.54 = B*0.02 + 0.95*P

Solve for P

620 = B + P .... P = 620-B

Then substitute in 620*0.54 = B*0.02 + 0.95*P

620*0.54 = B*0.02 + 0.95*(620-B)

Solve for B

334.8 = 0.02B + 589 - 0.95B

-0.93B = 334.8 -589

B = (334.8 -589 )/(-0.93 ) = 273.333 lbmolh = 273.33*0.454 = 124.09 kg/h

Solve for P

620 = B + P

620 = 273.333+ P

P = 620 - 273.333 = 346.667 lbmol/h = 346.667 *0.454 = 157.38 kg/h

calculate the fraction of benzene being fed

balance benzene

benzene in destillate = 0.98*273.33= 267.8634 lbmol/h (from those 285 lbmol/h being fed)

Know the answer?
Your Answer:

Post as a guest

Your Name:

What's your source?

Earn Coins

Coins can be redeemed for fabulous gifts.

Not the answer you're looking for?
Ask your own homework help question
Similar Questions
Separation Process: Suppose a saturated liquid feed of a benzene (B)/toluene (T) mixture (50 mol% B)...
Separation Process: Suppose a saturated liquid feed of a benzene (B)/toluene (T) mixture (50 mol% B) to a column is to be separated into a high purity distillate that is has a mole fraction of B equal to 0.9999 with a bottoms product mole fraction of 0.10. You may take the relative volatility to be aBT = 2.49 at the temperature that the column is operated. You are also given the reflux ratio to be 10.0, assuming a total condenser....
A mixture of Mol-100 kmol containing 70% benzene and 30% toluene must be separated at a...
A mixture of Mol-100 kmol containing 70% benzene and 30% toluene must be separated at a total pressure of 101.325 KPA (1 atm). A differential distillation column and an equilibrium(flash) distillation column are available in the enterprise to perform this operation. If 45 kmol distillate (top product) is obtained; a -) the composition of the distillate and remaining liquid obtained by differential distillation, B -) determine the composition of distillate and liquid obtained from equilibrium distillation. What distillation process would...
A mixture of 25 mol% benzene and 75% toluene with the flow rate of 200 kmol/hr...
A mixture of 25 mol% benzene and 75% toluene with the flow rate of 200 kmol/hr is to be flashed. The liquid product is 15 mol% benzene. The constant relative volatility (α) is 2.4. Determine the vapor flow rate (V) in kmol/hr.
Consider a distillation column that receives a feed of 500 kg/min of a mixture of benzene...
Consider a distillation column that receives a feed of 500 kg/min of a mixture of benzene and cyclohexane that is 55 mole % benzene. We wish to design the column so that the distillate has a composition that is 95 mole % benzene and contains 90 % of the benzene fed to the column. Calculate the distillate and bottoms flow rates (in kg/min) and the composition of the bottoms product in mole %.
A distillation column should separate benzene and toluene in a 30 t/h feed flow containing 40...
A distillation column should separate benzene and toluene in a 30 t/h feed flow containing 40 % benzene and 60 % toluene. The overhead product should be 97 % benzene and bottom product 98 % toluene. The molar reflux ratio RD = 3.5 and the saturated liquid feed has a boiling point of 95 °C. Calculate flow rates of distillate and bottom product . determine the number of ideal trays needed for the separation . Where is the feed tray...
A liq mixture of benzene-toluene is to be distilled in a fractionating tower at 101.3 kPa...
A liq mixture of benzene-toluene is to be distilled in a fractionating tower at 101.3 kPa pressure. The feed of 100 kg mol/h is liq and it contains 45 mole % benzene and 55 mole % toluene and enters at 327.6 K (130 ◦F). A distillate containing 95 mole % benzene and 5 mole % toluene and a bottoms containing 10 mole % benzene and 90 mole % toluene are to be obtained. The reflux ratio is 4:1. The average...
Rectification. McCabe-Thiele Method. A mixture of benzene-toluene is to be distilled in a fractionating tower at...
Rectification. McCabe-Thiele Method. A mixture of benzene-toluene is to be distilled in a fractionating tower at 101.3 kPa. The column is fed 120 kg mol /h of a saturated liquid at the boiling point with 60 mol % benzene and 40 mol % toluene. The content of the distillate is 92 mol % benzene, and of the bottoms 5 mol % benzene. The reflux ratio is 3:1. (a) Calculate the kg mol/h distillate: D=_______ (b) Calculate the kg mol/h bottoms:...
Q1. A mixture of toluene and benzene is to be separated continuously in a distillation column...
Q1. A mixture of toluene and benzene is to be separated continuously in a distillation column with the equilibria data provided in the table below. The required top product composition contains 95 mol% of benzene, and the bottom product composition contains 10 mol% of benzene. A feed consisting of 40 mol% benzene and 60 mol% toluene at its boiling point is fed to the column. Thermodynamic data: VLE data for Benzene & Toluene x 0 0.058 0.155 0.256 0.376 0.508...
A100 mol/h of feed mixture with 20% pentane, 25% hexane, 30% heptane and 25% octane is...
A100 mol/h of feed mixture with 20% pentane, 25% hexane, 30% heptane and 25% octane is to be distilled in a single column to an overall distillate product that contains no more than 2 mol/h of heptane and the bottom product that contains a maximum of 1.5 mol/h of hexane. Calculate the distillate and bottoms mole fraction, XDi and XBi, for all other components.
a mixture of 65 mol % n hexane and 35 mole % n octane is fed...
a mixture of 65 mol % n hexane and 35 mole % n octane is fed to a flash drum operating at 1500 mm Hg. Feed rate is 100 gmol/s. Mixture is heated to 110 degrees celcius, which the mixture vaporizes. Vapor and liquid products are removed constantly, A) Calculatae the vapor and liquid product compositions (Mol % n hexane and n octane) B) Calculate the vapor and liquid flow rates (gmol/s) y hex = 0.7 x hex = 0.6...
ADVERTISEMENT
Need Online Homework Help?

Get Answers For Free
Most questions answered within 1 hours.

Ask a Question
ADVERTISEMENT