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A Comparison of Simple Rheological Parameters and Simulation Data for Zymomonas mobilis Fermentation Broths with High Substrate Loading in a 3-L Bioreactor

机译:3-L生物反应器中高底物负载运动发酵单胞菌发酵液的简单流变参数和模拟数据的比较

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摘要

Traditionally, as much as 80% or more of an ethanol fermentation broth is water that must be removed. This mixture is not only costly to separate but also produces a large aqueous stream that must then be disposed of or recycled. Integrative approaches to water reduction include increasing the biomass concentration during fermentation. In this paper, experimental results are presented for the rheological behavior of high-solids enzymatic cellulose hydrolysis and ethanol fermentation for biomass conversion using Solka Floc as the model feedstock. The experimental determination of the viscosity, shear stress, and shear rate relationships of the 10 to 20% slurry concentrations with constant enzyme concentrations are performed with a variable speed rotational viscometer (2.0 to 200 rpm) at 40 °C. The viscosities of enzymatic suspension observed were in range of 0.0418 to 0.0144, 0.233 to 0.0348, and 0.292 to 0.0447 Pa s for shear rates up to 100 reciprocal seconds at 10, 15, and 20% initial solids (w/v), respectively. Computational fluid dynamics analysis of bioreactor mixing demonstrates the change in bioreactor mixing with increasing biomass concentration. The portion-loading method is shown to be effective for processing high-solids slurries.
机译:传统上,多达80%或更多的乙醇发酵液是必须去除的水。这种混合物不仅分离成本高昂,而且还会产生大量的水流,然后必须将其丢弃或回收。减少水分的综合方法包括增加发酵过程中的生物量浓度。本文以Solka Floc为模型原料,对高固体酶纤维素水解和乙醇发酵进行生物质转化的流变行为进行了实验研究。使用恒定转速的旋转粘度计(2.0至200 rpm)在40°C下进行10%至20%浆液浓度与恒定酶浓度的粘度,剪切应力和剪切速率关系的实验确定。在10%,15%和20%的初始固含量(w / v)下,剪切速率分别高达100倒数秒时,观察到的酶悬浮液的粘度分别为0.0418至0.0144、0.233至0.0348和0.292至0.0447 Pa s。生物反应器混合的计算流体动力学分析表明生物反应器混合随生物量浓度的增加而变化。事实表明,分装方法对于处理高固含量的浆料是有效的。

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