Anequimolarliquidmixtureofbenzeneandtolueneisseparatedintotwoproductstreamsbydistillation. A process flowchart and a somewhat oversimplified description of what happens in the process follow:
Feed
100 mol 0.500 mol B/mol 0.500 mol T/mol
n1(mol) n1(mol) CONDENSER
DISTILLATION COLUMN
Boilup yB[mol B(v)/mol]
Vaporâ97% mole benzene
Reflux
Overhead product
Bottoms product
REBOILER xB[mol B(l)/mol]
Inside the column a liquid stream flows downward and a vapor stream rises. At each point in the column some of the liquid vaporizes and some of the vapor condenses. The vapor leaving the top of the column, which contains 97 mole% benzene, is completely condensed and split into two equal fractions: one is taken off as the overhead product stream, and the other (the reflux) is recycled to the top of the column. The overhead product stream contains 89.2% of the benzene fed to the column. The liquid leaving the bottom of the column is fed to a partial reboiler in which 45% of it is vaporized. The vapor generated in the reboiler (the boilup) is recycled to become the rising vapor stream in the column, and the residual reboiler liquid is taken off as the bottom product stream. The compositions of the streams leaving the reboiler are governed by the relation
yB/1 ⣠yB 2:25 xB/1â£xB
where yB and xB are the mole fractions of benzene in the vapor and liquid streams, respectively. (a) Take a basis of 100 mol fed to the column. Draw and completely label a flowchart, and for each of four systems (overall process, column, condenser, and reboiler), do the degree-of-freedom analysis and identify a system with which the process analysis might appropriately begin (one with zero
degrees of freedom). (b) Write in order the equations you would solve to determine all unknown variables on the flowchart,
circling the variable for which you would solve in each equation. Do not do the calculations in this part. (c) Calculatethemolaramountsoftheoverheadandbottomsproducts,themolefractionofbenzenein the bottoms product, and the percentage recovery of toluene in the bottoms product (100 Ã moles
toluene in bottoms/mole toluene in feed).
Anequimolarliquidmixtureofbenzeneandtolueneisseparatedintotwoproductstreamsbydistillation. A process flowchart and a somewhat oversimplified description of what happens in the process follow:
Feed
100 mol 0.500 mol B/mol 0.500 mol T/mol
n1(mol) n1(mol) CONDENSER
DISTILLATION COLUMN
Boilup yB[mol B(v)/mol]
Vaporâ97% mole benzene
Reflux
Overhead product
Bottoms product
REBOILER xB[mol B(l)/mol]
Inside the column a liquid stream flows downward and a vapor stream rises. At each point in the column some of the liquid vaporizes and some of the vapor condenses. The vapor leaving the top of the column, which contains 97 mole% benzene, is completely condensed and split into two equal fractions: one is taken off as the overhead product stream, and the other (the reflux) is recycled to the top of the column. The overhead product stream contains 89.2% of the benzene fed to the column. The liquid leaving the bottom of the column is fed to a partial reboiler in which 45% of it is vaporized. The vapor generated in the reboiler (the boilup) is recycled to become the rising vapor stream in the column, and the residual reboiler liquid is taken off as the bottom product stream. The compositions of the streams leaving the reboiler are governed by the relation
yB/1 ⣠yB 2:25 xB/1â£xB
where yB and xB are the mole fractions of benzene in the vapor and liquid streams, respectively. (a) Take a basis of 100 mol fed to the column. Draw and completely label a flowchart, and for each of four systems (overall process, column, condenser, and reboiler), do the degree-of-freedom analysis and identify a system with which the process analysis might appropriately begin (one with zero
degrees of freedom). (b) Write in order the equations you would solve to determine all unknown variables on the flowchart,
circling the variable for which you would solve in each equation. Do not do the calculations in this part. (c) Calculatethemolaramountsoftheoverheadandbottomsproducts,themolefractionofbenzenein the bottoms product, and the percentage recovery of toluene in the bottoms product (100 Ã moles
toluene in bottoms/mole toluene in feed).
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