Sorry about that. #8 (20 pts) SO2 is to be removed from a CIL gas stream...
The heavier component has to be removed from a gas stream by absorption. The absorption column operates at 2 550 kPa. The entering liquid is high molecular mass oil which contains 0.45% of the heaviest component but none of the lighter components. The total molar flowrate of the oil entering the absorber is 150 kmol/hr. The effluent gas that enters the absorber at 800 kmolhr contains 20 mol% C, 46 mol% C2, 30 mol% C3, 4 mol% n-C4. There are...
#3 An absorber is to be used to remove acetone from air entering gas stream is 2 mole % acetone and enters at a rate of 40 kmol/hr. The water enters at a rate of 120 kmol hr. Both streams enter at 293 K and 1.4 atm pressure. We wish to remove 90 % of the entering acetone in this column. a. What is the minimum water flow to accomplish this separation? b. How many equilibrium stages would be required...
Please solve and I will rate answer A gas stream containing acetone in air flows from a solvent recovery unit at a rate of 142 L/s at 150°C and 1.3 atm. The stream flows into a condenser which condenses most of the acetone, and the liquid and gas outlet streams are in equilibrium at -18°C and 5.0atm. Shaft work is delivered to the system at a rate of 25.2kW to achieve the compression from 1.3 atm to 5.0 atm. To...
A stream containing ethane gas (C2He) enters the inner pipe of a double-pipe heat exchanger at 40°C and 105 kPa and exits from the pipe at 240*C and the same pressure. Superheated steam at 315 C and 5.0 bars enters the outer (annular) pipe, flowing counter-currently to the ethane, and exits as a saturated vapor at the same pressure. Neglecting the heat losses from the heat exchanger to its surroundings. Draw a diagram of the process. (5) What are the...