Design and structural parameter optimization of Venturi-type microbubble reactor for wastewater treatment by CFD simulation

IF 2 4区 化学 Q3 CHEMISTRY, MULTIDISCIPLINARY
Hanfei Liu, Chao Li, Shuangfei Zhao, Hao Zhu, Yiping Huang, Wei He, Yue Zhao, Yuguang Li, Kai Guo
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引用次数: 0

Abstract

Microbubble reactors play an important role in the development of gas-liquid reaction process enhancement. However, the urgent demand for high efficiency and low energy consumption in gas-liquid reaction processes, as well as the trend towards large-scale production, have put forward higher requirements for the design and optimization of microbubble reactors. In this study, a self-priming microbubble reactor was designed and its structure parameters were optimized by (computational fluid dynamics) CFD simulations. Based on the grid division method combining structured and unstructured grids, the most suitable mesh number is selected, and the simulation calculation time is saved on the premise of ensuring the accuracy. The effects of five structural parameters on the gas content and energy loss was discussed and the optimal structural parameters of the microbubble reactor were determined as follows: the diffusion section length is 75 mm, the contraction angle is 22°, the diffusion angle is 10.5°, the inlet diameter of the gas phase is 6 mm, the inlet diameter of the liquid phase flowing into the gas chamber is 3 mm, the diffusion section inlet diameter is 5 mm. Under the condition of the same inlet flow rate, the outlet gas content of the optimized gas-liquid reactor is increased by 42.9% compared with the initial structure. In the wastewater treatment experiment, the microbubble reactor reduced the chemical oxygen demand of wastewater by 61% within three hours. This study provides significant references for the design of the self-priming microbubble reactor.

Abstract Image

通过 CFD 仿真优化用于废水处理的文丘里型微气泡反应器的设计和结构参数
微气泡反应器在气液反应过程改进的发展中发挥着重要作用。然而,气液反应过程对高效率、低能耗的迫切需求以及大规模生产的趋势,对微泡反应器的设计和优化提出了更高的要求。本研究设计了一种自吸式微气泡反应器,并通过(计算流体动力学)CFD 仿真对其结构参数进行了优化。基于结构网格与非结构网格相结合的网格划分方法,选择了最合适的网格数,在保证精度的前提下节省了模拟计算时间。讨论了五个结构参数对气体含量和能量损失的影响,确定微气泡反应器的最佳结构参数如下:扩散段长度为 75 mm,收缩角为 22°,扩散角为 10.5°,气相入口直径为 6 mm,流入气室的液相入口直径为 3 mm,扩散段入口直径为 5 mm。在入口流速相同的条件下,优化后的气液反应器出口气体含量比初始结构提高了 42.9%。在废水处理实验中,微气泡反应器在三小时内使废水的化学需氧量降低了 61%。这项研究为自吸式微气泡反应器的设计提供了重要参考。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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来源期刊
Journal of Flow Chemistry
Journal of Flow Chemistry CHEMISTRY, MULTIDISCIPLINARY-
CiteScore
6.40
自引率
3.70%
发文量
29
审稿时长
>12 weeks
期刊介绍: The main focus of the journal is flow chemistry in inorganic, organic, analytical and process chemistry in the academic research as well as in applied research and development in the pharmaceutical, agrochemical, fine-chemical, petro- chemical, fragrance industry.
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