The following mixture of hydrocarbons is obtained as one stream in a peroleum refinery on a...
The following mixture of hydrocarbons is obtained as one stream in a peroleum refinery on a mole basis: 5% ethane, 10% propane, 40% n-butane, 45% isobutane. Assuming the shortcut K-ratio model.
1) compute the bubble point of the mixture at 5 bar.
2) compute the dew point of the mixture at 5 bar.
3) find the amounts and compositions of the vapor and liquid phases that would result if this mixture were to be isothermally flash vaporized at 30 degrees celcius from a high pressure to 5 bar.
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The following mixture of hydrocarbons is obtained as one stream
in a peroleum refinery on a...
2. Using K-values, determine a) The liquid phase composition of a ethane/propane mixture with a bubble...
2. Using K-values, determine a) The liquid phase composition of a ethane/propane mixture with a bubble point of -30 Fat 50 psia. b) The compositions of liquid and vapor phase for a system that, during a flash point separation at -30 °F at 50 psia splits into 40 mole % liquid and 60 mole % vapor.
Question 1.3: A mixture consisting of 1 mol-% ethane, 5 mol-% propane, 44 mol-% n-butane, and 50 mol-% isobutane is bro...
Question 1.3: A mixture consisting of 1 mol-% ethane, 5 mol-% propane, 44 mol-% n-butane, and 50 mol-% isobutane is brought to a condition of 70 °F at pressure 44 psia. Using De-Priester charts determine the molar fractions of the liquid and vapour phases and their compositions [3 marks]
Question 1.3: A mixture consisting of 1 mol-% ethane, 5 mol-% propane, 44 mol-% n-butane, and 50 mol-% isobutane is brought to a condition of 70 °F at pressure 44 psia....
For a mixture of 5% methane by mass 15% ethane by mass 30% propane and 50%...
For a mixture of 5% methane by mass 15% ethane by mass 30% propane and 50% n-butane by mass at 40 degrees Fahrenheit, determine the dew point presure and bubble point pressure. Vapor Pressures Methane - 19720.03 kPa Ethane - 2553. 95 kPa Propane - 541.1 kPa n-butane - 121.77 kPa
1. For the following T-X diagram for a mixture of A&B, do the following: (1) Show...
1. For the following T-X diagram for a mixture of A&B, do the following: (1) Show vapor, liquid and vapor-liquid region (2) Show bubble-point and dew-point line (3) Show tie line corresponding to 400 °F, 600 psia & 40 mole% A (4) Estimate boiling point of A (5) Estimate boiling point of B 6) Determine equilibrium vapor mole % for a mixture of 40 mole% B at 600 F & 600 psia (7) Determine the composition of vapor and liquid...
A stream of natural gas has the following composition by mole: methane = 70%, ethane=10%, propane...
A stream of natural gas has the following composition by mole: methane = 70%, ethane=10%, propane = 4% ,butane=10%, carbon dioxide = 6%. Calculate the the work to separate the mixture into its pure components at 24 ıC, 1 bar. Assume the mixture and the pure components to be in the ideal gas state. Miminum work is to be calculated.
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...
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...
The following feed mixture is to be separated by ordinary distillation at 120 psia so as to obtai...
Please answer the question D-E using the
K-value below
The following feed mixture is to be separated by ordinary distillation at 120 psia so as to obtain 92.5 mole% of the nc, in the liquid distillate and 82.0 mole% of the iC5 in the bottoms Lbmole/hr C3 iC nC ic nC 10 15 25 20 30 100 a) Estimate the minimum number of equilibrium stages required by applying the b) Use the Fenske equation to determine the distribution of nonkey...
Can someone explain me ..how they got the 29.o kg bda pls 254 Chapter 6 Multiphane...
Can someone explain me ..how they got the 29.o kg bda
pls
254 Chapter 6 Multiphane Sysicoms Percentage Saturation (Percentage Humidity) -n) × 100% ที่ (P-pp at a given temperature and pressure, you fraction of the vapor solve the defining equation to cakulate the partial peessure or mo ia the gas; thercafter, degrees of superheat. quantities for a gas If you are given amy of these q to given previously to calculate the dew point and you can use the...
2. Using K-values, determine a) The liquid phase composition of a ethane/propane mixture with a bubble point of -30 Fat 50 psia. b) The compositions of liquid and vapor phase for a system that, during a flash point separation at -30 °F at 50 psia splits into 40 mole % liquid and 60 mole % vapor.
Question 1.3: A mixture consisting of 1 mol-% ethane, 5 mol-% propane, 44 mol-% n-butane, and 50 mol-% isobutane is brought to a condition of 70 °F at pressure 44 psia. Using De-Priester charts determine the molar fractions of the liquid and vapour phases and their compositions [3 marks]
Question 1.3: A mixture consisting of 1 mol-% ethane, 5 mol-% propane, 44 mol-% n-butane, and 50 mol-% isobutane is brought to a condition of 70 °F at pressure 44 psia....
1. For the following T-X diagram for a mixture of A&B, do the following: (1) Show vapor, liquid and vapor-liquid region (2) Show bubble-point and dew-point line (3) Show tie line corresponding to 400 °F, 600 psia & 40 mole% A (4) Estimate boiling point of A (5) Estimate boiling point of B 6) Determine equilibrium vapor mole % for a mixture of 40 mole% B at 600 F & 600 psia (7) Determine the composition of vapor and liquid...
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...
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...
Please answer the question D-E using the
K-value below
The following feed mixture is to be separated by ordinary distillation at 120 psia so as to obtain 92.5 mole% of the nc, in the liquid distillate and 82.0 mole% of the iC5 in the bottoms Lbmole/hr C3 iC nC ic nC 10 15 25 20 30 100 a) Estimate the minimum number of equilibrium stages required by applying the b) Use the Fenske equation to determine the distribution of nonkey...
Can someone explain me ..how they got the 29.o kg bda
pls
254 Chapter 6 Multiphane Sysicoms Percentage Saturation (Percentage Humidity) -n) × 100% ที่ (P-pp at a given temperature and pressure, you fraction of the vapor solve the defining equation to cakulate the partial peessure or mo ia the gas; thercafter, degrees of superheat. quantities for a gas If you are given amy of these q to given previously to calculate the dew point and you can use the...
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