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#3 Ethyl acetate can be formed by the vapor-phase esterification of acetic acid

ID: 703769 • Letter: #

Question

#3 Ethyl acetate can be formed by the vapor-phase esterification of acetic acid and ethanol. This reaction was studied using a catalyst and found to be first order in ethanol and zeroth order in acetic acid with a specific reaction rate of 1.2 liter/g cat min. The total molar feed to a reactor is 10 mol/min, the initial pressure is 10 atm and the temperature is 391 K. Assume an equimolar feed and a pressure drop parameter,o, of 0.01/g. 1. Calculate the maximum weight of catalyst that could be used and still maintairn the reactor exit pressure above 1 atm. Determine the catalyst weight necessary to achieve 90 % conversion. 2,

Explanation / Answer

A) The rate of reaction is fist order in ethanol and zero order in acteic acid.

The rate of reaction is,

-rA = k CA CB° = kCA

Assume the reaction is Isothermal, so Epsolon = 0, P=Po/10

Therefor, P = Po(1-alpha W)^(1/2)

1 = 10(1-0.01W)^(1/2)

W = 99 g

B) Calculate weight of catalyst for 90% conversion.

Flow is equimolar, total flow is 10 mol/min. The molar flow of ethanol and acetic acid will be 5 mol/min each.

Calculate volumetric feed rate by calculating density of each feed stream at 10 atm and 391 K.

Total volumetric feed rate, FA0 = 32 L/min

Rate of reaction, -rA = kCA

CA = CA0 (1-X) P/Po

P/Po = (1- alpha W)^(1/2)

Therefore, CA = CAo (1-X) (1- alpha W)^(1/2)

Integrate X = 0 to X = 0.9

dX/dW = kCA (1-X) (1-alpha W)^(1/2)

FAo

ln(1/1-X) = (kCAo 2(1-(1-alpha W)^(3/2)) / (FAo 3alpha)

W = 81.43 gm