Question 2 Solids soaked with liquid hexane are dried by being contacted with nitrogen at an elevated temperature. The gas stream leaving the dryer is at 80°C, 1 atm absolute, and 50% relative...


Question 2<br>Solids soaked with liquid hexane are dried by being contacted with nitrogen at an elevated<br>temperature. The gas stream leaving the dryer is at 80°C, 1 atm absolute, and 50% relative<br>saturation.<br>a. One of several possibilities for recovering the hexane from the gas is to send the stream<br>to a cooling condenser. The gas stream leaving the condenser would contain 5.00<br>mole% hexane, and hexane condensate would be recovered at a rate of 1.50 kmol/min.<br>The condenser would be operated at a pressure of 1 atm absolute. Calculate the<br>temperature to which the gas must be cooled and the required flow rate of fresh nitrogen<br>to the dryer in standard cubic meters per minute (SCMM).<br>N2, high T<br>N2, 80°C, 1 atm<br>CONDENSER N2<br>(1 atm)<br>DRYER<br>CGH14 (s, = 50%)<br>CEH14 (v)(5 mole%)<br>Wet solids<br>Dry solids<br>1.5 kmol CEH14()/min<br>b. In an alternative arrangement, the gas leaving the dryer would be compressed to 10.0<br>atm and the temperature would simultaneously be increased so that the relative<br>saturation remains at 50%. The gas then would be cooled at constant pressure to<br>produce a stream containing 5.00 mole% hexane. Calculate the final gas temperature<br>and the ratio of volumetric flow rates of the gas streams leaving and entering the<br>condenser. State any assumptions you make.<br>

Extracted text: Question 2 Solids soaked with liquid hexane are dried by being contacted with nitrogen at an elevated temperature. The gas stream leaving the dryer is at 80°C, 1 atm absolute, and 50% relative saturation. a. One of several possibilities for recovering the hexane from the gas is to send the stream to a cooling condenser. The gas stream leaving the condenser would contain 5.00 mole% hexane, and hexane condensate would be recovered at a rate of 1.50 kmol/min. The condenser would be operated at a pressure of 1 atm absolute. Calculate the temperature to which the gas must be cooled and the required flow rate of fresh nitrogen to the dryer in standard cubic meters per minute (SCMM). N2, high T N2, 80°C, 1 atm CONDENSER N2 (1 atm) DRYER CGH14 (s, = 50%) CEH14 (v)(5 mole%) Wet solids Dry solids 1.5 kmol CEH14()/min b. In an alternative arrangement, the gas leaving the dryer would be compressed to 10.0 atm and the temperature would simultaneously be increased so that the relative saturation remains at 50%. The gas then would be cooled at constant pressure to produce a stream containing 5.00 mole% hexane. Calculate the final gas temperature and the ratio of volumetric flow rates of the gas streams leaving and entering the condenser. State any assumptions you make.

Jun 11, 2022
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