Atallah Al-Asad Hana, Parniske Janna, Qian Jueying, Alex Jens, Ramaswami Sreenivasan, Kaetzl Korbinian, Morck Tobias
University of Kassel, Department of Urban Water Engineering, Kurt-Wolters-Street 3, 34125, Kassel, Germany; ifak - Institute for Automation and Communication, Werner-Heisenberg-Str. 1, 39106, Magdeburg, Germany.
University of Kassel, Department of Urban Water Engineering, Kurt-Wolters-Street 3, 34125, Kassel, Germany.
Water Res. 2022 Jun 15;217:118427. doi: 10.1016/j.watres.2022.118427. Epub 2022 Apr 11.
This work presents a mathematical method to describe adsorptive removal of organic micropollutants (OMPs) and dissolved organic carbon (DOC) from wastewater treatment plant effluent using powdered activated carbon (PAC). The developed model is based on the tracer model (TRM) as a modification of the ideal adsorbed solution theory (IAST) and uses the fictive component approach for organic matter fractionation. It enables the simulation of multisolute adsorption of OMPs considering competitive adsorption behavior of organic background compounds (OBC). Adsorption equilibrium data for DOC and seven different OMPs as well as kinetic data for DOC were derived from batch experiments performed with secondary clarifier effluent of two municipal wastewater treatment plants (WWTP 1 and WWTP 2). Two conventional PAC products were investigated as well as one biogenic PAC (BioPAC). Verification and validation of the fitting results based on operational data of WWTP 1 showed promising prediction of DOC and OMP removal efficiency. However, when applied to a static simulation of a full-scale PAC adsorption stage, the model overpredicts the removal efficiency of sulfamethoxazole and candesartan. For benzotriazole, carbamazepine or hydrochlorothiazide, predicted removal falls below operational removal. The model can be used to predict removals of good adsorbable OMPs but fails to accurately predict the removals of OMPs with variable or low PAC affinity. The model was further used for a dynamic simulation of DOC and diclofenac effluent concentrations of a full-scale PAC adsorption stage with varying operating conditions and influent concentrations. Results show that the hydraulic retention time (HRT) in the contact reactor is a decisive operational parameter for OMP removal efficiency besides the PAC dose.
本研究提出了一种数学方法,用于描述使用粉末活性炭(PAC)从污水处理厂出水中吸附去除有机微污染物(OMPs)和溶解有机碳(DOC)的过程。所开发的模型基于示踪模型(TRM),它是对理想吸附溶液理论(IAST)的修正,并采用虚拟组分法对有机物进行分级。该模型能够模拟OMPs的多溶质吸附过程,同时考虑有机背景化合物(OBC)的竞争吸附行为。DOC和七种不同OMPs的吸附平衡数据以及DOC的动力学数据,均来自于对两个城市污水处理厂(WWTP 1和WWTP 2)二次沉淀池出水进行的间歇实验。研究了两种传统的PAC产品以及一种生物活性炭(BioPAC)。基于WWTP 1运行数据对拟合结果进行的验证和确认表明,该模型对DOC和OMP去除效率的预测效果良好。然而,当将其应用于全尺寸PAC吸附阶段的静态模拟时,该模型高估了磺胺甲恶唑和坎地沙坦的去除效率。对于苯并三唑、卡马西平或氢氯噻嗪,预测的去除率低于实际运行中的去除率。该模型可用于预测易于吸附的OMPs的去除情况,但无法准确预测与PAC亲和力可变或较低的OMPs的去除情况。该模型还进一步用于对全尺寸PAC吸附阶段在不同运行条件和进水浓度下的DOC和双氯芬酸出水浓度进行动态模拟。结果表明,除了PAC投加量外,接触反应器中的水力停留时间(HRT)是影响OMP去除效率的一个决定性运行参数。