电化学-膜分离耦合工艺处理变电站污水的减污降碳效能

Research on Electrochemical-Membrane Coupled Technology for Pollutant and Carbon Reduction in Substation Wastewater

  • 摘要: 随着变电站自动化、智能化水平的提高,站内污水排放逐渐呈现出水量小、排放不连续和水质波动较大的特征,尤其在我国东北等寒冷地区,低温环境进一步制约了传统生化处理工艺的稳定运行。针对该类污水处理需求,构建了电絮凝-电氧化-超滤/纳滤耦合工艺,系统考察其对化学需氧量(COD)、悬浮物(SS)、氨氮(NH3-N)和总磷(TP)等污染物的去除效果,并分析系统稳定性、水质波动适应性、间歇运行场景适用性及能耗特征。结果表明:电絮凝和电氧化单元的较优电流密度均为10 mA/cm2,在PAM和NaCl优化投加条件下,电化学单元对COD、SS、TP和NH3-N均表现出较好的去除效果,处理后出水COD < 50 mg/L、NH3-N < 5 mg/L,TP和SS降至较低水平;后续双膜单元进一步发挥了末端保障作用,在120 h连续运行过程中保持稳定膜通量,出水COD可进一步降至5 mg/L以下。针对较高污染负荷进水条件的实验结果表明,该组合工艺在水质波动条件下仍具有较好的出水保障能力和运行稳定性;间歇运行结果进一步说明,该体系对小水量、非连续排放场景具有较好的适应性。在较优运行条件下,出水中含氯消毒副产物总体处于较低水平,未表现出明显累积风险。系统吨水处理总能耗约为1.97 kWh/m3。总体来看,该电化学-膜分离耦合工艺适用于寒冷地区小规模、波动性较强的变电站污水处理场景,在实现污染物高效去除的同时,具有一定的工程应用和减污降碳潜力。

     

    Abstract: With the increasing automation and intelligence of substations, wastewater discharge has gradually become characterized by small volume, intermittent flow, and considerable water-quality fluctuation. In cold regions such as Northeast China, low temperatures further constrain the stable operation of conventional biological treatment processes. To address this challenge, an electrocoagulation-electrooxidation-ultrafiltration/nanofiltration coupled process was developed and systematically evaluated for the removal of chemical oxygen demand (COD), suspended solids (SS), ammonia nitrogen (NH3-N), and total phosphorus (TP), as well as for its operational stability, tolerance to water-quality fluctuation, applicability under intermittent operation, and energy consumption. The results showed that the optimal current density for both electrocoagulation and electrooxidation was 10 mA/cm2. Under optimized PAM and NaCl dosing conditions, the electrochemical units achieved effective removal of COD, SS, TP, and NH3-N, with electrochemically treated effluent COD below 50 mg/L and NH3-N below 5 mg/L, while TP and SS were reduced to very low levels. The subsequent dual-membrane unit provided further polishing, maintaining stable membrane flux over 120 h of continuous operation and reducing the final effluent COD to below 5 mg/L. Under high-pollution-load influent conditions, the coupled process still exhibited good effluent quality assurance and operational stability, indicating strong resistance to water-quality fluctuation. Intermittent operation tests further demonstrated its suitability for scenarios with small and discontinuous wastewater discharge. Under the optimized operating conditions, chlorinated disinfection by-products in the effluent remained at relatively low levels without obvious accumulation risk. The total energy consumption of the system was approximately 1.97 kWh/m3. Overall, the electrochemical-membrane coupled process is suitable for substation wastewater treatment in cold regions, especially for decentralized scenarios with strong water-quality fluctuation, and shows promising engineering applicability with pollutant reduction and potential carbon mitigation benefits.

     

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