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利用热微泡连续去除稀乙醇 - 水混合物中的乙醇

Continuous removal of ethanol from dilute ethanol-water mixtures using hot microbubbles.

作者信息

Calverley Joseph, Zimmerman William B, Leak David J, Hemaka Bandulasena H C

机构信息

Department of Chemical Engineering, Loughborough University, LE11 3TU, United Kingdom.

Department of Chemical and Biological Engineering, University of Sheffield, S1 3JD, United Kingdom.

出版信息

Chem Eng J. 2021 Nov 15;424:130511. doi: 10.1016/j.cej.2021.130511.

Abstract

Product inhibition is a barrier to many fermentation processes, including bioethanol production, and is responsible for dilute product streams which are energy intensive to purify. The main purpose of this study was to investigate whether hot microbubble stripping could be used to remove ethanol continuously from dilute ethanol-water mixtures expected in a bioreactor and maintain ethanol concentrations below the inhibitory levels for the thermophile (TM242), that can utilize a range of sugars derived from lignocellulosic biomass. A custom-made microbubble stripping unit that produces clouds of hot microbubbles (120 °C) by fluidic oscillation was used to remove ethanol from ~2% (v/v) ethanol-water mixtures maintained at 60 °C. Ethanol was continuously added to the unit to simulate microbial metabolism. The initial liquid height and the ethanol addition rate were varied from 10 to 50 mm and 2.1-21.2 g h respectively. In all the experiments, ethanol concentration was maintained well below the inhibition threshold of the target organism (2% [v/v]). This microbubble stripping unit has the potential to operate in conjunction with a 0.5-1.0 L fermenter to allow an ethanol productivity of 14.9-7.8 g L h continuously.

摘要

产物抑制是包括生物乙醇生产在内的许多发酵过程的障碍,并且导致了稀产物流,而这种稀产物流纯化起来能耗很高。本研究的主要目的是调查热微泡汽提法是否可用于从生物反应器中预期的稀乙醇 - 水混合物中连续去除乙醇,并将乙醇浓度维持在嗜热菌(TM242)的抑制水平以下,该嗜热菌能够利用一系列源自木质纤维素生物质的糖类。使用一个通过流体振荡产生热微泡云(约120°C)的定制微泡汽提装置,从保持在60°C的约2%(v/v)乙醇 - 水混合物中去除乙醇。向该装置中连续添加乙醇以模拟微生物代谢。初始液体高度和乙醇添加速率分别在10至50毫米和2.1 - 21.2克/小时之间变化。在所有实验中,乙醇浓度均保持在远低于目标生物体的抑制阈值(约2% [v/v])。这种微泡汽提装置有潜力与0.5 - 1.0升发酵罐联合运行,以实现连续14.9 - 7.8克/升·小时的乙醇生产率。

https://cdn.ncbi.nlm.nih.gov/pmc/blobs/9820/8447571/9b987bea85f7/gr1.jpg

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