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0One method of producing propylene is the dehydrogenation of propane (C3Hs) to propylene (CsHs) according to the reaction: A schematic of the reaction is shown below. The fresh feed (Stream 1) has a total flow rate of 100. mol/min and is composed of 96 mol% propane and 4.0 mol% propylene. The single pass conversion of propane across the reactor is 40% and all of the hydrogen is separated in the flash drum. Stream 5 exiting the flash drum is fed to a distillation column where 90% of the propylene is separated. The product (Stream 6) exiting the distillation column is composed of 99 mol% propylene and 1.0 mol% propane. The second stream exiting the column (Stream 7) is recycled back into the process a) Why is there no purge stream for this process? (5 points) fno impurities or excess reactants? b) What is the overall conversion of propane? (15 pts) (9996) c) What is the molar flow rate of propane in Stream 2? (10 pts) (238 mol/minj d) What is the molar flow rate of propylene in Stream 7? (10 pts) {llmol/min? e) What is the recycle to fresh feed ratio (Stream 7 / Stream 1)? (15pts) f1.5) f) Suggest 2 possible reasons why the single pass conversion of propane is relatively low. (5 points) fslowkinetics, reaction reaches equilibrium? Stream 7 Stream 3Flash drum Stream 1 Stream2 Stream 5 Reactor Column 100. mol/min 96% Propane 4.0% Propylene Stream4 Stream 6 100% Hydrogen 1.0% Propane 99% Propylene

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