in Wiley InterScience (www.interscience.wiley.com).
The isomerization of D-glucose to D-fructose using the immobilized glucose isomerase, as a typical model system of solid-liquid enzyme reactions has been carried out in a novel type of two-impinging-jets reactor (TIJR), which is characterized by a rotating inner cylinder in a stationary one. Because of the impinging process, turbulence, and complex trajectory of the solid particles within the reactor, the fractional conversion of glucose obtained in the TIJR increased dramatically compared to that obtained by conventional reaction systems. A compartment model was considered to describe the pattern of flow [residence time distribution (RTD) of solid particles] within the TIJR. Considering such a flow pattern, a stochastic model for the RTD of the solid particles was developed using Markov chains models. The latter was correlated with the experimental RTD data, obtained by using a tracer analysis technique. © 2005 American Institute of ChemicalEngineers AIChE J, 52: 692-704, 2006 Keywords: impinging jets, opposed jets, glucose isomerase, enzymatic isomerization, residence time distribution
IntroductionSolid-liquid enzyme reactions constitute important processes in biochemical industries. Among the latter, the isomerization of glucose to fructose is one of the most widely used processes in the food industry in producing dietetic "light" foods and drinks because it improves the sweetening, color, and hygroscopic characteristics in addition to reducing viscosity. Also, fructose is about 75% sweeter than sucrose, is absorbed more slowly than glucose, and is metabolized without the intervention of insulin. For all these reasons, this process is widely studied both with cells and with enzymes, both free and immobilized (IE). [1][2][3][4][5][6][7][8][9][10][11][12][13] From the perspective of chemical kinetics, isomerization of glucose to fructose is a reversible reaction, with an equilibrium constant of approximately unity at 55°C. 14 The heat of reaction is on the order of 5 kJ/mol 14 and, consequently, the equilibrium product contains roughly a 1:1 ratio of glucose to fructose that does not change appreciably with temperature, such that at 55°C the fructose content at equilibrium is 50%, and at higher temperatures such as 60, 70, 80, and 90°C is 50.7, 52.5, 53.9, and 55.6%, respectively. However, increasing temperature decreases stability and the enzyme half-life and therefore productivity. Most industrial plants run at 58 -60°C, a temperature with low risk for microbial contamination.The process was originally carried out in batch reactors with soluble enzymes. It was later extended to one involving immobilized glucose isomerase (IGI), which is of interest to us in the present work. In addition to the aforementioned batch reactors, there are various types of enzyme reactors, including continuous stirred tank reactors (CSTR), fixed-bed reactors, simulated moving beds, and fluidized-bed reactors. In the fixed-and fluidized-bed reactors, the enzymes are immobilized ...