A continuous fractionation column is to be designed to separate 20000 kg / hr of a mixture of 40% benzene and 60% toluene into a distillate containing 97% benzene and a residual product of 96% toluene. These percentages are expressed by weight. A reflux ratio of 3.5 moles per 1 mole of product will be used. The molar latent heats of benzene and toluene are 7360 and 7960 cal / mol, respectively. Benzene and toluene form an ideal system with a relative volatility of the order of 2.5. The feed has a boiling point of 95 ° C at a pressure of 1 atm. i. Calculate the moles of distilled and residual products per hour ii. Calculate Qr and QC. Feed is a liquid at 20 ° C (specific heat = 0.44 cal / g ° C)

Introduction to Chemical Engineering Thermodynamics
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Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
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A continuous fractionation column is to be designed to separate 20000 kg / hr of a mixture of 40% benzene and 60% toluene into a distillate containing 97% benzene and a residual product of 96% toluene. These percentages are expressed by weight. A reflux ratio of 3.5 moles per 1 mole of product will be used. The molar latent heats of benzene and toluene are 7360 and 7960 cal / mol, respectively. Benzene and toluene form an ideal system with a relative volatility of the order of 2.5. The feed has a boiling point of 95 ° C at a pressure of 1 atm.

i. Calculate the moles of distilled and residual products per hour

ii. Calculate Qr and QC.

Feed is a liquid at 20 ° C (specific heat = 0.44 cal / g ° C)

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