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使用生物催化剂在气升式反应器中从空气中捕获二氧化碳的计算流体动力学建模。

Computational fluid dynamics modeling of carbon dioxide capture from air using biocatalyst in an airlift reactor.

机构信息

Department of Chemical Engineering, University of Sistan and Baluchestan, Zahedan, P.O. Box. 98164-161, Iran.

Department of Chemical Engineering, University of Sistan and Baluchestan, Zahedan, P.O. Box. 98164-161, Iran.

出版信息

Bioresour Technol. 2018 Apr;253:154-164. doi: 10.1016/j.biortech.2018.01.025. Epub 2018 Jan 8.

Abstract

In this work, a novel three-phase and three dimensional CFD model based on the Euler-Euler approach developed for modeling the hydrodynamic, mass transfer and CO fixation using microalgae in an internal loop airlift reactor with internal sparger. The main objective of this work was to development of CFD codes in order to simulate the CO biofixation process under different input gas velocity during 11 days of culture time and simulate the unsteady state mass transfer based on Surface-Renewal-Stretch (SRS) model. The CFD results were compared with the our previous experimental work and they showed good agreement with a margin of less than 10%. This paper illustrated the ability of the CFD in complex process simulation such as CO biofixation in the airlift reactor and provided a useful basis for further study.

摘要

在这项工作中,开发了一种基于欧拉-欧拉方法的新型三相三维 CFD 模型,用于在带有内部喷射器的内部环升力反应器中使用微藻进行水动力、传质和 CO 固定的建模。这项工作的主要目的是开发 CFD 代码,以便在 11 天的培养时间内模拟不同输入气体速度下的 CO 生物固定过程,并基于表面更新拉伸(SRS)模型模拟非稳态传质。CFD 结果与我们之前的实验工作进行了比较,它们之间的一致性很好,误差在 10%以内。本文说明了 CFD 在复杂过程模拟中的能力,例如在升力反应器中的 CO 生物固定,并为进一步研究提供了有用的基础。

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