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新型旋流除乳化空气升液环式反应器处理精炼大豆油废水的计算流体力学及因子分析

Computational fluid dynamics and factor analysis of a novel swirling demulsified airlift loop reactor for the treatment of refined soybean oil wastewater.

机构信息

Sci-Tech Center for Clean Conversion and High-valued Utilization of Biomass, Jilin Province, Northeast Electric Power University, Jilin 132012, China; School of Chemical Engineering, Northeast Electric Power University, Jilin 132012, China.

Sci-Tech Center for Clean Conversion and High-valued Utilization of Biomass, Jilin Province, Northeast Electric Power University, Jilin 132012, China.

出版信息

Bioresour Technol. 2020 Jan;296:122316. doi: 10.1016/j.biortech.2019.122316. Epub 2019 Oct 22.

Abstract

A swirling demulsified airlift loop reactor (SD-ALR) was developed for the treatment of oily wastewater with yeasts. Computational fluid dynamics simulations showed that the gas holdup and liquid velocity gradient in the SD-ALR were 2.9% and 0.37 m/s higher than those in the traditional airlift loop reactor. The optimization results of the swirling demulsifier showed that the optimal number and elevation angle of the blades were 8 and 45°, and the optimal installation position was 150 mm from the bottom of the draft tube. The results of treating refined soybean oil wastewater in the SD-ALR showed that the wastewater treatment time was decreased by 8 h, and the removals of chemical oxygen demand and oil content increased by 5.10% ± 0.02% and 9.55% ± 0.40%, respectively, compared with those in the traditional airlift loop reactor. A volumetric mass transfer coefficient model was established for SD-ALR and oily wastewater.

摘要

旋流消泡空气提升环式反应器(SD-ALR)用于处理含酵母的含油废水。计算流体动力学模拟表明,SD-ALR 中的气含率和液体速度梯度分别比传统空气提升环式反应器高 2.9%和 0.37m/s。旋流消泡器的优化结果表明,叶片的最佳数量和仰角为 8 和 45°,最佳安装位置是距底管 150mm。在 SD-ALR 中处理精炼大豆油废水的结果表明,与传统空气提升环式反应器相比,废水处理时间缩短了 8h,化学需氧量和油含量的去除率分别提高了 5.10%±0.02%和 9.55%±0.40%。建立了用于 SD-ALR 和含油废水的容积传质系数模型。

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