Water recovery from cleaning wastewater of traditional Chinese medicine processing via vacuum membrane distillation: Parameters optimization and membrane fouling investigation

被引:7
|
作者
Zhang, Yansong [1 ]
Ji, Zheng [1 ]
Yan, Haiyang [1 ]
Wu, Bo [1 ]
Guo, Yanyan [1 ]
Wang, Huchuan [1 ]
Li, Chuanrun [1 ,2 ]
机构
[1] Anhui Univ Chinese Med, Pharmaceut Engn Technol Res Ctr, Sch Pharm, Hefei 230012, Anhui, Peoples R China
[2] Anhui Prov Key Lab Pharmaceut Preparat Technol & A, Hefei 230012, Anhui, Peoples R China
来源
关键词
Vacuum membrane distillation; Traditional Chinese medicine; Water recovery; Membrane fouling; Membrane cleaning; REACTOR; REGENERATION; DESALINATION; PERFORMANCE; BIOREACTOR; SUBSTANCES; MODEL;
D O I
10.1016/j.cherd.2022.10.010
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
With the rapid development of traditional Chinese medicine (TCM) industry, the treat-ment of TCM wastewater has become an important environmental issue. Among them, TCM processing cleaning wastewater is suitable for recovering high-quality water re-sources from it due to its low chemical oxygen demand (COD). Compared with pressure driven membrane process, Membrane distillation (MD) can yield highly purified distillate under mild operating conditions. Therefore, this work aims to evaluate the effects of feed temperature, feed flow, osmotic side vacuum degree and membrane material on the treatment of cleaning wastewater from TCM processing. Besides, the fouling of membrane in MD process and the efficiency of chemical cleaning on fouling removal were also in-vestigated. The results show that it is feasible to recover high-quality water from tradi-tional Chinese medicine processing cleaning wastewater by VMD. Compared with feed, COD in permeate decreased by 99%. During the 10 h experiment, the flux of both mem-branes decreased slightly due to the accumulation of fouling layer on the membrane surface. Chemical cleaning, especially alkali as cleaning agent can effectively remove the fouling layer. (c) 2022 Institution of Chemical Engineers. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:555 / 563
页数:9
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