Problem 4.40 Sequential Distillation A liquid mixture containing 30.0 mole% benzene (B), 25.0% toluene (T), and...
Problem 4.40 Sequential Distillation A liquid mixture containing 30.0 mole% benzene (B), 25.0% toluene (T), and the balance xylene (X) is fed to a distillation column. The bottoms product contains 98.0 mole% X and no B, and 85.5% of the X in the feed is recovered in this stream. The overhead product is fed to a second column. The overhead product from the second column contains 91.0% of the B in the feed to this column. The composition of this stream is 94.0 mole% B and the balance T. Write three balances and use one constraint for the performance of Still 1 to solve for the following quantities for a process feed (n1) of 100.0 mol/h. First Still Bottoms flow rate (n2) = mol/h. Overhead fow rate (n3) = mol/h. Benzene mole fraction in overhead (X3B) = .Toluene mole fraction in overhead (X3T) = .
Still 2 Write three balances and use one constraint for the performance of Still 2 to solve for the following quantities for a process feed (n1) of 100.0 mol/h. Second Still . Overhead from second still (n5) = mol/h. Bottoms from second still ( n4) = mol/h . Benzene mole fraction in bottoms from second still (X4B) = . Toluene mole fraction in bottoms from second still (X4T) =. question part Recovery. Calculate the percentage of B in the process feed that is recovered in the overhead of the second distialltion column = %. Calculate the percentatge of T in the process feed that is recovered in the bottoms of the second distillation column = %.
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Problem 4.40 Sequential Distillation A liquid mixture containing
30.0 mole% benzene (B), 25.0% toluene (T), and...
An equimolar liquid mixture of benzene and toluene is separated into two product streams by distillation....
An equimolar liquid mixture of benzene and toluene is separated into two product streams by distillation. A process flowchart and a somewhat oversimplified description of what happens in the process follow: Vapor-97% mole benzene A Reflux Overhead product Filmoi) 24 CONDENSER", mot Feed 100 mol 0.500 mol Bimal La DISTILLATION 0.500 mol/mol Bollup mol B[/mol) 1 Bottoms product REBOILER mol B/D/mol Inside the column a liquid stream flows downward and a vapor stream rises. At each point in the column...
4.42. An equimolar liquid mixture of benzene and toluene is separated into two product streams by...
4.42. An equimolar liquid mixture of benzene and toluene is separated into two product streams by distillation. A process flowchart and a somewhat oversimplified description of what happens in the process follow: Vapor-97% mole benzene Overhead product Reflux n(mol) n1(mol) CONDENSER Feed 100 mol DISTILLATION COLUMN 0.500 mol B/mol 0.500 mol T/mol Boilup yBmol B(v)/mol] Bottoms product REBOILER *B[mol B(1)/mol] Inside the column a liquid stream flows downward and a vapor stream rises. At each point in the column some...
A liquid mixture containing 45.0 % benzene (B) and 55.0 % toluene (T) by mass is...
A liquid mixture containing 45.0 % benzene (B) and 55.0 % toluene (T) by mass is fed to a distillation column. A product stream leaving the top of the column (the overhead product) contains 95.0 mole % B, and a bottom product stream contains 8.0 % of the benzene fed to the column (meaning that 92% of the benzene leaves with the overhead product). the volumetric flow rate of the feed stream is 2000 L/h and the specific gravity of...
A distillation column is fed with a liquid mixture of 25.0 mole % benzene, 30 %...
A
distillation column is fed with a liquid mixture of 25.0 mole %
benzene, 30 % toluene and 45 % xylene. The bottom product from the
distillation column contains 97 mole % xylene and no benzene. The
other stream (upper one) contains 29 % benzene and it is fed to a
second distillation column. The upper...
Problem 2. A distillation column is fed with a liquid mixture of 25.0 mole benzene, 30 toluene, and 45 xylene. The bottom product from...
A mixture containing 45% benzene (B) and 55% toluene (T) by mass is fed to a...
A mixture containing 45% benzene (B) and 55% toluene (T) by mass is fed to a distillation column an overhead stream of 95% B is produced, and 8% of the benzene fed to the column leaves in the bottom stream. The feed rate is 2000kg/h. 1- suggest the suitable material to fabricate the distillation column. 2-Ideentify the corrosive behavior of chemicals to the selected material and calculate the corrosive allowance for thickness of the column. 3-Explain the suitable maintenance procedure...
A mixture containing 42% benzene and 58% toluene by mass is fed to a distillation column....
A mixture containing 42% benzene and 58% toluene by mass is fed to a distillation column. A second mixture is also fed to the distillation column and has a composition of 65% toluene and 35% acetone by mass. The flowrates of the mixtures are 2500 kg h1 and 1500 kg h1 respectively. An overhead distillate exit stream of 800 kg h-1 containing 23% acetone and a bottom exit stream of 25% benzene are produced. Determine the bottom exit flowrate and...
HW3 Differential Distillation of Benzene-Toluene. A mixture containing 70 mol % benzene and 30 mol %...
HW3 Differential Distillation of Benzene-Toluene. A mixture containing 70 mol % benzene and 30 mol % toluene is distilled under differential conditions at 101.32 kPa (1 atm). A total of one third of the moles in the feed is vaporized. Calculate the average composition of the distillate and the composition of the remaining liquid. Use equilibrium data in Table 11.1-1. given as mole fraction n-heptane. 0.284 0.097 0.067 0.459 0.184 0.131 0.039 0.012 0.078 0.025
A saturated liquid feed with a composition of 45 mole-% benzene and 55 mole-% toluene is...
A saturated liquid feed with a composition of 45 mole-% benzene and 55 mole-% toluene is distilled in a plate column at the rate of 250 kmol/h. Overhead product contains 97 mole-% benzene and the bottom product contains 5 mole-% benzene. A total condenser and a partial reboiler are used. The reflux ratio employed is 1.5 times the minimum, RD 1.5 RDmin Find the number of theoretical plates required for this separation, the heat duties of the condenser and reboiler....
A gas containing nitrogen, benzene, and toluene is in equilibrium with a liquid mixture of 40...
A gas containing nitrogen, benzene, and toluene is in equilibrium with a liquid mixture of 40 mol% benzene and 60 mol% toluene at 80°C and 21 atm a) Calculate the gas phase mole fraction of benzene. (8 points) b) Calculate the gas phase mole fraction of toluene. (8 points c) Calculate the volumetric flow rate (L/s) of the gas mixture if it were being continuously removed from the process at a rate of 200 mol/s. (Do not assume the gas...
Toluene + H2 → Benzene + CH4 Two streams enter the process. The first input stream...
Toluene + H2 → Benzene + CH4 Two streams enter the process. The first input stream is pure liquid toluene, which enters at a rate of 40 mol/s. The second input stream is a mixture of H2 (95 mole%) and CH4 (5 mole%). The flow rate of H2 in the second stream is equal to 200 mol/s. Two streams leave the process. The first output stream contains only liquid benzene (product) and toluene (unconverted reactant). The second output stream contains...
An equimolar liquid mixture of benzene and toluene is separated into two product streams by distillation. A process flowchart and a somewhat oversimplified description of what happens in the process follow: Vapor-97% mole benzene A Reflux Overhead product Filmoi) 24 CONDENSER", mot Feed 100 mol 0.500 mol Bimal La DISTILLATION 0.500 mol/mol Bollup mol B[/mol) 1 Bottoms product REBOILER mol B/D/mol Inside the column a liquid stream flows downward and a vapor stream rises. At each point in the column...
4.42. An equimolar liquid mixture of benzene and toluene is separated into two product streams by distillation. A process flowchart and a somewhat oversimplified description of what happens in the process follow: Vapor-97% mole benzene Overhead product Reflux n(mol) n1(mol) CONDENSER Feed 100 mol DISTILLATION COLUMN 0.500 mol B/mol 0.500 mol T/mol Boilup yBmol B(v)/mol] Bottoms product REBOILER *B[mol B(1)/mol] Inside the column a liquid stream flows downward and a vapor stream rises. At each point in the column some...
A
distillation column is fed with a liquid mixture of 25.0 mole %
benzene, 30 % toluene and 45 % xylene. The bottom product from the
distillation column contains 97 mole % xylene and no benzene. The
other stream (upper one) contains 29 % benzene and it is fed to a
second distillation column. The upper...
Problem 2. A distillation column is fed with a liquid mixture of 25.0 mole benzene, 30 toluene, and 45 xylene. The bottom product from...
A mixture containing 42% benzene and 58% toluene by mass is fed to a distillation column. A second mixture is also fed to the distillation column and has a composition of 65% toluene and 35% acetone by mass. The flowrates of the mixtures are 2500 kg h1 and 1500 kg h1 respectively. An overhead distillate exit stream of 800 kg h-1 containing 23% acetone and a bottom exit stream of 25% benzene are produced. Determine the bottom exit flowrate and...
HW3 Differential Distillation of Benzene-Toluene. A mixture containing 70 mol % benzene and 30 mol % toluene is distilled under differential conditions at 101.32 kPa (1 atm). A total of one third of the moles in the feed is vaporized. Calculate the average composition of the distillate and the composition of the remaining liquid. Use equilibrium data in Table 11.1-1. given as mole fraction n-heptane. 0.284 0.097 0.067 0.459 0.184 0.131 0.039 0.012 0.078 0.025
A saturated liquid feed with a composition of 45 mole-% benzene and 55 mole-% toluene is distilled in a plate column at the rate of 250 kmol/h. Overhead product contains 97 mole-% benzene and the bottom product contains 5 mole-% benzene. A total condenser and a partial reboiler are used. The reflux ratio employed is 1.5 times the minimum, RD 1.5 RDmin Find the number of theoretical plates required for this separation, the heat duties of the condenser and reboiler....
A gas containing nitrogen, benzene, and toluene is in equilibrium with a liquid mixture of 40 mol% benzene and 60 mol% toluene at 80°C and 21 atm a) Calculate the gas phase mole fraction of benzene. (8 points) b) Calculate the gas phase mole fraction of toluene. (8 points c) Calculate the volumetric flow rate (L/s) of the gas mixture if it were being continuously removed from the process at a rate of 200 mol/s. (Do not assume the gas...
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