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Enzymatic Catalysis and Electrostatic Process Intensification for Processing of Natural Oils

机译:酶促催化和静电过程加强加工天然油

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The work described here is concerned with the enhancement of liquid - liquid contact of oil/water mixtures using high voltage electrical fields. The enzymatic hydrolysis of high oleate sunflower oil was studied in an electrically enhanced liquid-liquid reactor. The kinetics of the reaction were measured at a range of applied electrical field strengths. The effect of electrical field upon liquid hold-up was also determined. The performance of a laboratory scale electrically enhanced enzymatic reactor was evaluated in batch mode, in recycle mode and in continuous mode of operation. The results of the study showed that the rate of reaction was significantly enhanced as the magnitude of the applied electrical field was increased. The dispersed phase hold-up in the recycle reactor was reduced at increased electrical field strength and the rate of phase separation enhanced. The enhanced interfacial area generated by electrostatic dispersion was one factor in the observed increase in the reaction rate. However the specific rates of reaction (rate of conversion per unit interfacial area) for electrical dispersions showed a very large increase when compared with dispersions of similar quality which were generated by mechanical agitation. A clear difference in the rate of reaction for a negative electrical field was also observed when compared with a positive electrical field.
机译:这里描述的工作涉及使用高压电场提高油/水混合物的液体液体接触。在电增强液 - 液反应器中研究了高油e葵花油的酶水解。在一系列施加的电场强度下测量反应的动力学。还确定了电场对液体封闭时的影响。在批量模式下,在循环模式和连续操作模式下评估实验室电增强酶反应器的性能。该研究的结果表明,随着所施加的电场的幅度增加,反应速率显着增强。在循环反应器中的分散相载体以增加的电场强度和相分离速率增强。通过静电分散体产生的增强的界面区域是观察到的反应速率增加的一个因素。然而,与通过机械搅拌产生的类似质量的分散体相比,电分散时间的特定反应率(每单位界面区域)的电分散率显示出非常大的增加。与正电场相比,还观察到负电场反应速率的明显差异。

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