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Separation of benzene and toluene A column at 101 kPa is to separate 30 kgh of a bubble pointsolution of benzene and toluene containing 06 mass fraction tolueneinto an overhead product of

Separation of benzene and toluene A column at 101 kPa is to separate 30 kgh of a bubble pointsolution of benzene and toluene containing 06 mass fraction tolueneinto an overhead product of

Separation of benzene and toluene.A column at 101 kPa is to separate 30 kg/h of a bubble-pointsolution of benzene and toluene containing 0.6 mass-fraction tolueneinto an overhead product of 0.97 mass-fraction benzene anda bottoms product of 0.98 mass-fraction toluene at a reflux ratioof 3.5. The feed is sent to the optimal tray, and the reflux is at saturationtemperature. Determine the: (a) top and bottom products and(b) number of stages using the following vapor–liquid equilibriumdata.

rahul 18-Jul-2020

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