首页> 外文期刊>Biochemical Engineering Journal >Mass transfer characterization in forward and back extractions of lysozyme by AOT-isooctane reverse micelles across a flat liquid-liquid interface
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Mass transfer characterization in forward and back extractions of lysozyme by AOT-isooctane reverse micelles across a flat liquid-liquid interface

机译:AOT-异辛烷反胶团在平坦液-液界面上向前和向后提取溶菌酶的传质特性

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摘要

The mass transfer rates in lysozyme extraction between an aqueous KCl solution and an bis (2-ethyl) sodium sulfosuccinate (AOT)-isooctane reversed micellar solution were investigated using a stirred cell with a flat liquid-liquid interface. The forward extraction rates from 0.1 kmol m~(-3) KCl solution of pH 6.5 to a reversed micellar phase are controlled by the diffusion in the aqueous film and the solubilization at the interface. The solubilizing rate constant, k_(fs), increases from 3.57*10~(-5) to 1.43*10~(-4) m s~(-1) in proportion to AOT concentration of 0.05 to 0.2 kmol m~(-3). Forthe back extraction of lysozyme from the reversed micellar phase to an aqueous solution of higher KCl concentration,the rate-determining step is the release process at the interface. The releasing rate constant, k_(bd),decreases with an increase of AOT concentration and is also two orders smaller than the k_(fs) values. The back extraction rates are therefore very slow compared to the forward extraction rates.
机译:使用具有平坦液-液界面的搅拌池研究了在KCl水溶液和双(2-乙基)磺基琥珀酸钠(AOT)-异辛烷反胶束溶液之间进行溶菌酶萃取的传质速率。 pH值为6.5的0.1 kmol m〜(-3)KCl溶液正向萃取胶束相的正向萃取速率由水膜中的扩散和界面处的增溶作用控制。溶解速率常数k_(fs)与AOT浓度0.05至0.2 kmol m〜(-3)成比例,从3.57 * 10〜(-5)增加到1.43 * 10〜(-4)ms〜(-1) )。为了将溶菌酶从逆胶束相反萃取到较高KCl浓度的水溶液中,决定速率的步骤是界面处的释放过程。释放速率常数k_(bd)随着AOT浓度的增加而减小,并且也比k_(fs)值小两个数量级。因此,与正向提取速率相比,反向提取速率非常慢。

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