There is a 2-m3 reactor in storage that is to be used to carry out the liquid-phase second-order reaction
A and B are to be fed in equimolar amounts at a volumetric rate of 1 m3/min. The entering concentration of A is 2 molar, and the specific reaction rate is 1.5 m3/kmol · min. A tracer experiment was carried out and reported in terms of F as a function of time in minutes as shown in Figure P18-17B.
Figure P18-17B F-curve for a nonideal reactor.
Suggest a two-parameter model consistent with the data; evaluate the model parameters and the expected conversion.
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Elements of Chemical Reaction Engineering (5th Edition) (Prentice Hall International Series in the Physical and Chemical Engineering Sciences)
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