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Large-scale synthesis of dihydrostreptomycin via hydrogenation of streptomycin in a membrane dispersion microreactor

机译:膜分散微反应器中氢化链霉素氢化二氢霉素的大规模合成

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Highlights?A novel method for the preparation of dihydrostreptomycin.?Conversion rate (99.5%) of streptomycin were reached in 3?min.?The difference between the microreactor and the traditional stirring tank was investigated.?The effect of the pH of the aqueous solution and other factors was investigated.AbstractIn this work, a membrane dispersion microreactor was applied for the hydrogenation of streptomycin (STR) to produce dihydrostreptomycin (DHS). The reductant was dispersed into the continuous phase containing STR, leading to a significant increase in the mass-transfer specific surface area, and the conversion rate of STR reached 99.81?wt% within 3?min. In contrast, in stirred tanks, the conversion rate of STR only reached 99.5% in 30?min. Moreover, the minimum amount of KBH4used in the membrane dispersion microreactor was about 35.71% lower than that in traditional tanks, when achieving the same conversion rate at about 99.5%.]]>
机译:<![cdata [ 亮点 一种制备二氢霉素的新方法。 转换率(99.5%)链霉素的转化率(99.5%)在3?分钟内。 研究了微反应器和传统搅拌罐之间的差异。 水溶液的pH的效果和其他因素的效果呕吐。 抽象 < CE:简单 - 段ID =“SP0010”视图=“全部”>在这项工作中,施加膜分散微反应器用于氢化链霉素(str)以产生二氢霉素(DHS)。将还原剂分散到含连续的含量中,导致质量转移比表面积显着增加,ST的转化率达到99.81〜wt%在3?min内。相比之下,在搅拌罐中,STR的转化率仅达到30.5%的30?min。此外,在膜分散微反应器中使用的kbh 4 在传统坦克中的相同转化率约为99.5时,在膜分散微反应器中的最小值约为35.71%。 %。 ]]>

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