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Study of suspension condition of yeast flocs in air lift bioreactor for ethanol fermentation

机译:气浮生物反应器中酵母絮凝物悬浮条件的乙醇发酵研究。

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In this paper, the design principles and characteristics of biroreactor using yeast flocs was introduced, and the minimum air input for the suspension of yeast flocs was studied. The research showed that the air input calculated according to the formula established on a 12L bioreactor in reference (1) can not match the experiment result in the scale up of biroeactors(2.35L, 500L, 10000L) for ethanol production usign yeast flocs, but after the influence of the difference of solid fraction on the both sides of the draft tube was taken into account in the momentum balance equation, the air input required to suspend the yeast flocs and maintain the circulation of the media in the bioreactor can be well predicted by the formula in the scale up the bioreactors, thus it can be well concluded that the resistance force caused by solid fraction difference on both sides of the draft tube can not be neglected, further calculation showed that it is the main resistance to be overcome by the air input. at critical liquid circulation speed in bioreactors large than 12L, although the friction force may becoem strogner at high circulation speed.
机译:本文介绍了使用酵母絮状物的双反应器的设计原理和特点,并研究了悬浮酵母菌的最小空气输入量。研究表明,根据参考文献(1)中使用12升生物反应器建立的公式计算出的空气输入量无法与将双反应器(2.35升,500升,10000升)用于生产酵母菌絮的规模扩大的实验结果相匹配,但是在动量平衡方程中考虑了固相分数差异对引流管两侧的影响之后,可以很好地预测悬浮酵母絮并维持生物反应器中培养基循环所需的空气输入量。通过放大生物反应器中的公式,可以很好地得出结论,引流管两侧固相分数差异所引起的阻力不能忽略,进一步的计算表明,这是需要克服的主要阻力。空气输入。在大于12L的生物反应器中,在临界液体循环速度下,尽管摩擦力可能在高循环速度下成为斯托格纳。

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