Abstract
The article reports numerical simulation for the system combining selective adsorption of fructose and an enzyme reaction to produce higher fructose syrup. A procedure for the dynamic simulation of the process in the frame of equations for mass transfer in fixed bed, is obtained by making a solute material balance. A fixed bed model incorporating axial dispersion and a linear driving force for mass transfer was successfully used to estimate optimum operating conditions (switch times and fluid flow rates)
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