Question

A countercurrent absorption column operating at 3 atm and 20 °C is used to scrub acetone...

  1. A countercurrent absorption column operating at 3 atm and 20 °C is used to scrub acetone from air into water. Separation is to be accomplished in 5 equilibrium stages. The total inlet gas flow rate is 100 kmol/h and contains 0.4 mol% acetone. The inlet liquid contains 0.01 mol% acetone. Outlet gas is 0.02 mol% acetone. Assume constant flow rates and note that the Henry’s law constant (H) for acetone in water at 20 °C is 1.186 atm/(mole fraction). Find the liquid flow rate required and the mole fraction acetone in the outlet liquid.

Homework Answers

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
A process off-gas flow contains 1,4 mol-% acetone, when the gas flow rate is 2,20 kmol/min....
A process off-gas flow contains 1,4 mol-% acetone, when the gas flow rate is 2,20 kmol/min. The acetone should be removed to achieve a concentration of 0,070 mol-% acetone in the outlet gas flow. The gas is washed with pure water with a flow rate 1,05 kmol/min. Calculate the acetone concentration (mol-%) of the spent washing liquid and the flow rate (mol/min) of acetone flowing from the gas phase to the aqueous phase
In a gas absorption tower, acetone is absorbed from its mixture with air using a nonvolatile...
In a gas absorption tower, acetone is absorbed from its mixture with air using a nonvolatile absorption oil. 100 mol/h of gas mixture enter the bottom of the column contains 30 mol% acetone while 261.9 mol/h oil enter the top of the column. The exiting gas stream is to contain 1.3 mol% acetone. a) Determine molar flow rate of the exiting gas and exiting liquid streams. b) Determine number of stages required for the above process.
In the absorption of component A (molecular weight = 60 g/mol) from an airstream into an...
In the absorption of component A (molecular weight = 60 g/mol) from an airstream into an aqueous solution, the bulk compositions of the two adjacent streams at a point in the apparatus were analyzed to be PA,G = 0.1 atm and CA,L = 1 kmol of A/m3 . The Henry’s Law constant was 0.85 ATM/mole fraction. The overall gas coefficient was KG = 0.27 kmol/m2/h/ATM. If 60% of the total resistance to mass transfer resides in the gas film, determine:...
We are absorbing hydrogen sulfide at 15°C into water. The entering water is pure. The feed...
We are absorbing hydrogen sulfide at 15°C into water. The entering water is pure. The feed gas contains 0.0012 mole frac hydrogen sulfide and we want to remove 97% of this in the water. The total gas flow rate is 10 kmol/h. The total liquid flow rate is 2000 kmol/h. Total pressure is 2.5 atm. You can assume that total liquid and gas flow rates are constant. Equilibrium data are in Table 12-1. a. Calculate the outlet gas and liquid...
1) Calculating Number of Stages in Counter-Current Stripping with Tray Towers: A counter current steam stripper...
1) Calculating Number of Stages in Counter-Current Stripping with Tray Towers: A counter current steam stripper has a liquid stream containing 0.02 mol % nitrobenzene in water. Entering steam is pure water. Outlet mole fraction of nitrobenzene in liquid is 0.00001. Assuming dilute species with constant liquid and gas flow rates. Equilibrium can be represented as Y = 28*X (a) Calculate minimum vapor flow rate (V’min) to perform the operation, given L’ = 1000 kmol/hr. (b) Given L’/V’ = 12;...
Separation of Acetone and Ethanol A distillation column with a total condenser and partial reboiler is...
Separation of Acetone and Ethanol A distillation column with a total condenser and partial reboiler is separating acetone and ethanol (equilibrium data is provided in the table below). The feed is 70 mole% acetone, flows at 1000 mol/h, and is a superheated vapor for which one mole of liquid must be vaporized on the feed plate to cool four moles of feed. We desire a bottoms composition of 5 mole% acetone and a distillate composition of 90 mole% acetone. The...
It is desired to absorb ammonia from air into water producing an outlet gas stream with...
It is desired to absorb ammonia from air into water producing an outlet gas stream with 0.5mol% ammonia. equilibrium data given as y=1.414x in mole fraction. The counter current column has three equilibrium stages. Entering gas stream has a total of 10 kgmole/hr and has 80% mil NH3. Inlet water stream contains 2% mil ammonia. Find required flow rate entering liquid stream and flow rate of all outlet stream.
Species A can react to species B in the gas phase (A --> B) with the...
Species A can react to species B in the gas phase (A --> B) with the equilibrium constant K. A flow system feeds 2 mol/min of A to a reactor that reaches equilibrium. The total pressure in the reactor is maintained at 1 bar. K is equal to 7. a. What are the mole fractions of A and B leaving the reactor? b. What are the exit flow rates of A and B leaving the reactor? c. A liquid that...
A fuel gas produced by gasifying coal is to be burned with 20% excess air. The...
A fuel gas produced by gasifying coal is to be burned with 20% excess air. The gas contains 50.0 mole % nitrogen and the balance carbon monoxide and hydrogen. A sample of the gas is passed through an infrared spectrometer, which registers a signal R that depends on the mole fraction of carbon monoxide in the sample, and a reading R 38:3 is recorded. Analyzer calibration data are as follows: x (mol CO/mol) 0.05 0.10 0.40 0.80 1.00 R 10.0...
A fuel gas produced by gasifying coal is to be burned with 20% excess air. The...
A fuel gas produced by gasifying coal is to be burned with 20% excess air. The gas contains 50.0 mole % nitrogen and the balance carbon monoxide and hydrogen. A sample of the gas is passed through an infrared spectrometer, which registers a signal R that depends on the mole fraction of carbon monoxide in the sample, and a reading R 38:3 is recorded.  Analyzer calibration data are as follows: x (mol CO/mol) 0.05 0.10 0.40 0.80 1.00 R 10.0 17.0...