纳滤-粉末活性炭混合系统进一步处理 A2O-MBR 处理的焦化废水

Elif İnce, M. Ince, Furkan Durmaz, Handenur Yasar, Yasin Abdullah Uslu
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摘要

缺氧-缺氧膜生物反应器(A2O-MBR)是处理焦化废水所需的生物系统之一,在钢铁工业不断发展的影响下,该系统的使用量有所增加;然而,由于废水中存在难降解的污染物,该系统无法达到土耳其共和国环境、城市化和气候变化部(CSB)规定的排放标准。为使焦化废水经 A2O-MBR 高级处理后达到该部的标准,研究了纳滤(NF)(两种不同的膜和不同的压力)、粉末活性炭-微滤(PAC-MF)和 PAC-NF(两种不同的膜和五种不同的 PAC 浓度)。除了该部确定的参数外,还调查了其他参数(氨、硫氰酸盐(SCN-)、氰化氢(HCN)、溶解有机碳(DOC)、溶解无机碳(DIC)、色度),以评估混合工艺的通量性能和处理效率。结果表明,NF 工艺中的化学需氧量 (COD)、PAC-MF 工艺中的 COD 和总氰化物 (T-CN) 均未达到排放标准。在 PAC-NF 混合系统中,XN45 的所有参数(COD = 96 ± 1.88 mg/L、T-CN = <0.02 mg/L、酚 = <0.05 mg/L)均达到排放标准,在 PAC 浓度为 0.5 g/L 时,回收率为 78%。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Further treatment of coking wastewater treated in A2O-MBR by the nanofiltration-powder activated carbon hybrid system
Anoxic–oxic membrane bioreactor (A2O-MBR), one of the biological systems requently used for the treatment of coking wastewater, increased under the influence of the growing iron and steel industry; however it cannot meet the discharge standards set by the Ministry of Environment, Urbanization and Climate Change of the Republic of Türkiye (CSB) due to recalcitrant pollutants in the wastewater. Advanced treatment of coking wastewater treated in A2O-MBR to meet the standards of the Ministry; nanofiltration (NF) (two different membranes and different pressures), powder activated carbon-microfiltration (PAC-MF), and PAC-NF (two different membranes and five different PAC concentrations) were investigated. In addition to the parameters determined by the Ministry, other parameters (ammonium, thiocyanate (SCN−), hydrogen cyanide (HCN), dissolved organic carbon (DOC), dissolved inorganic carbon (DIC), color) were also investigated to evaluate the performance of flux and treatment efficiency of the hybrid process. According to the results, chemical oxygen demand (COD) in the NF process, COD, and total cyanide (T-CN) in the PAC-MF process could not meet the discharge standards. In the PAC-NF hybrid system, XN45 met the discharge standards in all parameters (COD = 96 ± 1.88 mg/L, T-CN = <0.02 mg/L, phenol = <0.05 mg/L), with a 78% recovery rate at 0.5 g/L PAC concentration.
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