roday. A mixture of air and acetone enter a condenser at 255 OC and 1.1 bar with partial pressure of acetone is 0.100 bar. A portion of the acetone is liquefied and the effluent gas leaves at 10 OC...


roday.<br>A mixture of air and acetone enter a condenser at 255 OC and 1.1 bar with partial pressure<br>of acetone is 0.100 bar. A portion of the acetone is liquefied and the effluent gas leaves at<br>10 OC and 40 bar. The air leaving the condenser at partial pressure of 0.621 bar. Assume<br>ideal<br>gas<br>behavior.<br>a. Calculate for a basis of 2.5 m3 of gas fed to the condenser the mass of acetone condensed (kg) and<br>the volume of gas leaving the condenser (m3).<br>b. Suppose the volumetric flow rate of the gas leaving the condenser is 35.0 m3/h.<br>Calculate the rate (kg/h) at which acetone is vaporized in the solvent recovery unit.<br>

Extracted text: roday. A mixture of air and acetone enter a condenser at 255 OC and 1.1 bar with partial pressure of acetone is 0.100 bar. A portion of the acetone is liquefied and the effluent gas leaves at 10 OC and 40 bar. The air leaving the condenser at partial pressure of 0.621 bar. Assume ideal gas behavior. a. Calculate for a basis of 2.5 m3 of gas fed to the condenser the mass of acetone condensed (kg) and the volume of gas leaving the condenser (m3). b. Suppose the volumetric flow rate of the gas leaving the condenser is 35.0 m3/h. Calculate the rate (kg/h) at which acetone is vaporized in the solvent recovery unit.

Jun 11, 2022
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