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首页> 外文期刊>Biochemical Engineering Journal >Gas-liquid mass transfer studies with triple impeller system on a laboratory scale bioreactor
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Gas-liquid mass transfer studies with triple impeller system on a laboratory scale bioreactor

机译:在实验室规模的生物反应器上使用三叶轮系统进行气液传质研究

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摘要

The gas-liquid mass transfer coefficient K_La in a fermentor is known to be a strong function of the mode of energy dissipation and physicochemical properties of the liquid media.Three impeller combinations namely,single,double and triple impellers,respectively have been tested in the laboratory bioreactor (21) for their gas-liquid mass transfer performance.The liquid phase physico-chemical properties have been varied using distilled water,aqueous solutions of sodium carboxymethyl cellulose and simulated fermentation medium.The effects of the process variables such as the impeller speed,gas flow rate and the liquid phase physico-chemical properties on the volumetric liquid phase mass transfer coefficient of oxygen,K_La in a stirred bioreactor were investigated by static gassing out method.Correlations have been developed for the predictions of the gas-liquid mass transfer coefficient with liquids having different physico-chemical properties.It has been observed that triple impeller system gave highest values of gas-liquid mass transfer coefficient with the least power consumption.
机译:众所周知,发酵罐中的气液传质系数K_La与液体介质的能量耗散模式和物理化学特性有很强的函数关系。在单叶轮,双叶轮和三叶轮中分别测试了三种叶轮组合。实验室生物反应器(21)的气液传质性能。使用蒸馏水,羧甲基纤维素钠水溶液和模拟发酵介质改变了液相的理化性质。叶轮转速等工艺变量的影响静态排气法研究了搅拌生物反应器中气体的流速和液相物理化学性质对氧气体积液相传质系数K_La的影响。为预测气液传质建立了相关性具有不同理化性质的液体的系数。已经观察到三叶轮系统tem以最小的功耗给出了最高的气液传质系数值。

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