混凝—磁分离—电化学技术处理压裂返排液研究

对页岩气开采中压裂返排液的组成、特性及处理现状进行分析,提出采用破胶混凝—磁分离—电化学催化氧化技术处理压裂返排液。研究得到各处理单元优化工艺,其中破胶混凝工艺采用高铁酸钾破胶剂、投加量2 500 mg/L,混凝剂聚合氯化铝铁投加量为2 000 mg/L,反应p H为11.0,反应时间40 min;磁分离工艺采用纳米磁铁粉,投加量4 000 mg/L,高分子絮凝剂阴离子聚丙烯酰胺投加量为20 mg/L;电化学催化氧化工艺采用Ti/Ti O_2作阳极,不锈钢作阴极,氧化电压10.0 V,电流密度1.6×10-2 A/cm2,体系p H为11.0,反应时间30 min。研究结果表明,采用上述技术及优化工艺处理压裂返排液,处理后COD、SS、油、色度、p H等主要指标均达到GB 8978—2002的一级排放标准要求。

Research on the treatment of fracturing flow-back fluid by coagulation-magnet separation-electrochemistry combined technology

The components,characteristics and treatment actuality of fracturing flow-back fluid from shale gas explo-ration are analyzed. It is put forward that the gel-breaking coagulation-magnetic separation-electrochemistry catalysis oxidation technology is used for treating fracturing flow-back fluid. The optimized technology of every treatment unit is obtained through researches,among which gel-breaker K2FeO4 is used in the gel-breaking coagulation process. The conditions needed are as follows:the dosage of K2FeO4 is 2 500 mg/L,PAFC dosage 2 000 mg/L, reacting pH 11.0 and reaction time 40 min. Nano-magnet powder 4 000 mg/L and polymer flocculant HPAM 20 mg/L are needed for the magnetic separation process. Ti/TiO2 plate is used as anode,while stainless steel plate as cathode, oxidation voltage 10.0 V,current density1.6×10-2 A/cm2,reaction pH of the system 11.0 and reaction time 30 min are needed for the electrochemistry catalysis oxidation process. The research results show that after the above technology and optimized processes have been used for the treatment of fracturing flow-back fluid,all of the main factors,such as COD,SS,oil content,chroma,pH,etc. meet the requirements specified in the first class of the Integrated Wastewater Discharge Standard(GB 8978—2002).