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电渗析耦合升流式厌氧污泥床和膜生物反应器处理精制糖废水的研究

Study on the Treatment of Refined Sugar Wastewater by Electrodialysis Coupled with Upflow Anaerobic Sludge Blanket and Membrane Bioreactor.

作者信息

Xu Shichang, Zhao Han, Xie Lixin, Wang Keqiang, Zhang Wen

机构信息

School of Chemical Engineering and Technology, Tianjin Key Laboratory of Membrane Science and Desalination Technology, State Key Laboratory of Chemical Engineering (Tianjin University), Tianjin University, Tianjin 300350, China.

出版信息

Membranes (Basel). 2023 May 19;13(5):527. doi: 10.3390/membranes13050527.

Abstract

In this paper, refined sugar wastewater (RSW) is treated by electrodialysis (ED) coupled with an upflow anaerobic sludge blanket (UASB) and membrane bioreactor (MBR). The salt in RSW was first removed by ED, and then the remaining organic components in RSW were degraded by a combined UASB and MBR system. In the batch operation of ED, the RSW was desalinated to a certain level (conductivity < 6 mS·cm) at different dilute to concentrated stream volume ratios (V/V). At the volume ratio of 5:1, the salt migration rate and COD migration rate were 283.9 g·h·m and 13.84 g·h·m, respectively, and the separation factor (defined as ) reached a minimum value of 0.0487. The ion exchange capacity () of ion exchange membranes (IEMs) after 5 months of usage showed a slight change from 2.3 mmol·g to 1.8 mmol·g. After the ED treatment, the effluent from the tank of the dilute stream was introduced into the combined UASB-MBR system. In the stabilization stage, the average COD of UASB effluent was 2048 mg·L, and the effluent COD of MBR was maintained below 44-69 mg·L, which met the discharge standard of water contaminants for the sugar industry. The coupled method reported here provides a viable idea and an effective reference for treating RSW and other similar industrial wastewaters with high salinity and organic contents.

摘要

本文采用电渗析(ED)结合上流式厌氧污泥床(UASB)和膜生物反应器(MBR)处理精制糖废水(RSW)。首先通过电渗析去除RSW中的盐分,然后利用UASB和MBR组合系统降解RSW中剩余的有机成分。在电渗析的间歇操作中,RSW在不同的稀相流与浓相流体积比(V/V)下被脱盐至一定水平(电导率<6 mS·cm)。在体积比为5:1时,盐迁移速率和COD迁移速率分别为283.9 g·h·m和13.84 g·h·m,分离因子(定义为)达到最小值0.0487。使用5个月后的离子交换膜(IEMs)的离子交换容量从2.3 mmol·g略微变化至1.8 mmol·g。电渗析处理后,稀相流罐中的流出物被引入UASB-MBR组合系统。在稳定阶段,UASB流出物的平均COD为2048 mg·L,MBR的流出物COD保持在44 - 69 mg·L以下,符合制糖工业水污染物排放标准。本文报道的耦合方法为处理RSW和其他类似的高盐度和高有机物含量的工业废水提供了可行的思路和有效的参考。

https://cdn.ncbi.nlm.nih.gov/pmc/blobs/8bdb/10224370/7c1b449c7b77/membranes-13-00527-g001.jpg

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