3. The working charge of a four foot adsorption bed is 32.0%. The MTZ and heel were determined to be 2 inches and 2.3%, respectively. Calculate the saturation capacity. a. 41.9% b. 36.6% c. 35.0% d. 32.0%

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3. The working charge of a four foot adsorption bed is 32.0%. The MTZ and heel were
determined to be 2 inches and 2.3%, respectively. Calculate the saturation capacity.
a. 41.9%
b. 36.6%
c. 35.0%
d. 32.0%
4. How many pounds of carbon would be needed to remove 150 lb/hr of benzene from
an air stream (1 atm, 77°F) containing 0.68% by volume toluene. The adsorber
operates on a 2 hour adsorption cycle and the working charge can be estimated by
doubling the amount of carbon needed at the saturation capacity. The saturation
capacity of carbon for benzene with a partial pressure in the 0.05-0.12 psia range is
approximately 0.40 lb B/lb AC.
a. 750
b. 1000
c. 1500
d. 2000
Transcribed Image Text:3. The working charge of a four foot adsorption bed is 32.0%. The MTZ and heel were determined to be 2 inches and 2.3%, respectively. Calculate the saturation capacity. a. 41.9% b. 36.6% c. 35.0% d. 32.0% 4. How many pounds of carbon would be needed to remove 150 lb/hr of benzene from an air stream (1 atm, 77°F) containing 0.68% by volume toluene. The adsorber operates on a 2 hour adsorption cycle and the working charge can be estimated by doubling the amount of carbon needed at the saturation capacity. The saturation capacity of carbon for benzene with a partial pressure in the 0.05-0.12 psia range is approximately 0.40 lb B/lb AC. a. 750 b. 1000 c. 1500 d. 2000
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