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3 . 1 9 b . Material balances: adsorption of benzene vapor on activated carbon; cocurrent operation If the adsorption process described in Problem 3

3.19b. Material balances: adsorption of benzene vapor on activated carbon; cocurrent operation
If the adsorption process described in Problem 3.17 took place cocurrently, calculate the minimum flow rate of activated carbon required.
Answer: 0.543kgs
3.17?b. Material balances: adsorption of benzene vapor on activated carbon
Activated carbon is used to recover benzene from a nitrogenbenzene vapor mixture. The mixture, at 306K and 1atm containing 1.0% benzene by volume, is to be passed countercurrently at the rate of 1.0m3s to a moving stream of activated carbon so as to remove 85% of the benzene from the gas in a continuous process. The entering activated carbon contains 15cm3 of benzene vapor (at STP) adsorbed per gram of the carbon. The temperature and total pressure are maintained at 306K and 1atm. Nitrogen is not adsorbed.
a. Plot the equilibrium data given in the table below as x'=kg benzene ?kg dry carbon, Y'=kg benzene ?kg nitrogen for a total pressure of 1atm.
b. Calculate the minimum flow rate required of the entering carbon (remember that the entering carbon contains some adsorbed benzene).
Answer: 0.096kg of activated carbon/s
c. If the carbon flow is 20% above the minimum, what will be the concentrationof benzene adsorbed on the carbon leaving the process?
Answer: 0.295kg benzene/kg activated carbon
d. For the conditions of part (c), calculate the number of ideal stages required.
Answer: 3.32 stages
\table[[\table[[Benzene vapor adsorbed,],[cm3(STP)/g of carbon]],\table[[mm Hg],[(STial pressure of benzene,]]],[15,0.55],[25,0.95],[40,1.63],[50,2.18],[65,3.26],[80,4.88],[100,6.22]]
The equilibrium adsorption of benzene on this activated carbon at the temperature of 306K is reported as follows:
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