Calculate the product compositions, stage temperatures, interstage flow rates and compositions, and reboiler duty for the re-boiled
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Calculate the product compositions, stage temperatures, interstage flow rates and compositions, and reboiler duty for the re-boiled stripper shown in Figure10.40.
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Overhead vapor Feed 39.2°F, 150 psia Ibmol/h 0.22 N2 150 psia 59.51 73.57 153.22 173.22 58.22 33.63 Ca nCg Bottoms 99.33 Ibmol/h
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