Department of Chemical Engineering, Lund University, PO Box 124, SE-221 00 Lund, Sweden; Sweden Water Research AB, Ideon Science Park, Scheelevägen 15, SE-223 70 Lund, Sweden.
Department of Chemical Engineering, Lund University, PO Box 124, SE-221 00 Lund, Sweden.
Sci Total Environ. 2022 Mar 10;811:152225. doi: 10.1016/j.scitotenv.2021.152225. Epub 2021 Dec 16.
The adsorption of organic micropollutants onto powdered activated carbon (PAC) was investigated in laboratory scale based on samples from four wastewater process streams (matrices); three from a pilot-scale plant with different degrees of physicochemical treatment of municipal wastewater and one from a full-scale activated sludge plant with post-precipitation. The pilot-scale treatment consisted of chemically enhanced primary treatment with microsieving followed by direct membrane filtration as microfiltration or ultrafiltration. The results showed highest adsorption of micropollutants in the tertiary (biologically and chemically) treated wastewater and lowest adsorption in the microsieve filtrate. Adsorption of micropollutants in the direct membrane microfiltration (200 nm) permeate was generally similar to that in the direct membrane ultrafiltration (3 nm) permeate. The higher adsorption of micropollutants in the tertiary treated wastewater could be related to a lower concentration of dissolved organic carbon (DOC) and lower affinity of DOC for PAC at low dosage (<15 mg PAC/L) in this matrix. At a PAC dose of 10 mg/L, sulfamethoxazole was removed by 33% in the tertiary treated wastewater and 7% in the direct membrane microfiltration permeate. In addition to the PAC experiments, a pilot scale sand filter and a proceeding GAC filter was operated on tertiary treated wastewater from the full-scale treatment plant. Similar removal trends in the PAC and GAC experiments were observed when studying a weighted average micropollutant removal in the GAC filter and a similar dose of activated carbon for both PAC and GAC. Positively charged micropollutants were removed to a higher extent than negatively charged ones by both PAC and GAC.
基于来自四个废水处理流程(基质)的样本,研究了粉末活性炭(PAC)对有机微量污染物的吸附作用,这是在实验室规模上进行的。四个基质中有三个来自具有不同程度的物化处理的市政污水的中试规模工厂,还有一个来自具有后沉淀的全规模活性污泥厂。中试处理包括用微筛进行化学增强的一级处理,然后直接进行膜过滤,作为微滤或超滤。结果表明,在三级(生物和化学)处理的废水中,微量污染物的吸附最高,而在微筛滤出物中的吸附最低。直接膜微滤(200nm)透过物中微量污染物的吸附通常与直接膜超滤(3nm)透过物中的吸附相似。在三级处理的废水中,微量污染物的高吸附可能与低浓度的溶解有机碳(DOC)和在这种基质中低剂量(<15mgPAC/L)下DOC对 PAC 的低亲和力有关。在 PAC 剂量为 10mg/L 时,磺胺甲恶唑在三级处理废水中的去除率为 33%,而在直接膜微滤透过物中的去除率为 7%。除了 PAC 实验外,中试规模的砂滤器和正在运行的 GAC 过滤器也在全规模处理厂的三级处理废水中运行。在研究 GAC 过滤器中的加权平均微量污染物去除率和 PAC 和 GAC 的相似剂量的活性炭时,在 PAC 和 GAC 实验中观察到相似的去除趋势。PAC 和 GAC 都对正电荷的微量污染物的去除程度高于负电荷的微量污染物。