Studies in nanofiltration of dyes industry effluent

IF 0.9 Q4 ENGINEERING, CHEMICAL Indian Chemical Engineer Pub Date : 2023-03-04 DOI:10.1080/00194506.2023.2190321
Pritesh S. Patil, N. Thombre, Yagna Prasad K., A. Patwardhan
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Abstract

ABSTRACT A large number of chemicals are being produced in the industries, which resulted in accumulation in the effluent stream. The impact of these effluents on the environment is very adverse, if it released directly without treatment. Nowadays, the treatment of the effluent before discharge is very important due to strict norms imposed by various government agencies. In our study, the effluent from a local effluent treatment plant (effluent from dyes factory) was procured and treated with hydrophilic polymeric and ceramic nanofiltration membranes. The membrane characterisation was done based on flux, permeability, flux recovery ratio, and flux decline ratio. The effluent received from ETP and treated effluent was characterised in terms of pH, total dissolved solids (TDS), Chemical Oxygen Demand (COD), Conductivity, Turbidity, and Osmolality. From our experimental study, more encouraging results were obtained. More than 50% COD reduction was observed in the process. The membrane flux was recovered by the physical (by using backwashing) and chemical process (by using sodium hypochlorite solution). The different range was used for optimising the appropriate process for recovery of membrane flux. About 95% membrane flux was recovered by physical process on both ceramic and polymeric membranes. GRAPHICAL ABSTRACT
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染料工业废水的纳滤研究
摘要工业生产中产生了大量的化学物质,这些化学物质在废水中积累。如果未经处理直接排放,这些废水对环境的影响是非常不利的。如今,由于各政府机构实施了严格的规范,污水排放前的处理非常重要。在我们的研究中,采购了当地污水处理厂的污水(染料厂的污水),并用亲水性聚合物和陶瓷纳滤膜进行处理。基于通量、渗透率、通量恢复率和通量下降率对膜进行了表征。根据pH、总溶解固体(TDS)、化学需氧量(COD)、电导率、浊度和渗透压来表征从ETP接收的流出物和经处理的流出液。从我们的实验研究中,获得了更令人鼓舞的结果。在该过程中观察到COD降低了50%以上。通过物理(通过反冲洗)和化学过程(通过使用次氯酸钠溶液)回收膜通量。不同的范围用于优化膜通量回收的适当工艺。在陶瓷膜和聚合物膜上,通过物理处理回收了约95%的膜通量。图形摘要
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来源期刊
Indian Chemical Engineer
Indian Chemical Engineer ENGINEERING, CHEMICAL-
CiteScore
3.00
自引率
6.70%
发文量
33
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