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Study on the Microaerobic EGSB Reactor+Chemical Coagulation System Treating Domestic Wastewater

机译:微生虫EGSB反应器+化学凝固系统治疗家庭废水的研究

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A novel domestic wastewater treatment system for reuse was proposed, which consisted of a microaerobic EGSB reactor unit and the following chemical phosphorus removal unit, as a low-cost and highly efficient process. In order to confirm the feasibility of the domestic wastewater treating technique at ambient temperature for reuse through the combination of the micro-aerobic EGSB reactor and the chemical phosphorus removal process, the operation characteristic of the microaerobic EGSB reactor was analyzed. Moreover, the final chemical precipitations with aluminium sulphate, PAC, ferric trichloride and PES were employed to enhance the TP removal from the micro-aerobic EGSB system. Studies were focused on the influences of flocculation and settling time, coagulant dosage, pH and temperature on the effluent TP removal of the microaerobic EGSB reactor. The resulted showed that the microaerobic EGSB reactor treating domestic wastewater run well at 15-26°C. And at the conditions of 2.5-3.1L·h~(-1) influent flow, 3.9-4.8h HRT, 2.2-2.9mh~(-1) Vup, with influent COD, NH_3-N, TN and TP concentration of 213-1145, 26.5-72.1,31.7-81.7 and 3.9-16.3mg·h~(-1), the effluent COD, NH_3-N, TN and TP concentratios were 26.3, 9.9,14.0 and 4.7mg·L~(-1), and which was up to the IA, IB, IA and EI distinction standard of GB 18918-2002, respectively. Subsequently, it was essential to enhance the TP removal of the micro-aerobic EGSB reactor effluent through chemical precipitation. The optimal "β" (the mole ratio of Al~(3+): P or Fe~(3+):P) for aluminium sulphate, PAC, ferric trichloride and PES was 1.1, 6.9, 3.1 and 2.1, and meanwhile 20, 10, 20 and 15min flocculation time were selected, respectively. And in succession, sedimentating with 20min, the minimum TP removal efficiency of 85%, 90.8%, 92% and 92% could attain, and the effluent TP was under the value of 0.71, 0.43, 0.38 and 0.38mg·L~(-1), respectively, and which had accorded with the IA distinction standard of GB 18918-2002 except for the aluminium sulphate. It was compulsory for the 0.5mg·L~(-1) TP distinction standard to adjust the pH. Consenquently, the domestic wastewater treating technique at ambient temperature for reuse through the combination of the micro-aerophilic EGSB reactor and the chemical phosphorus removal process is feasible.
机译:提出了一种用于再利用的新型污水处理系统,其由微生物EGSB反应器单元和以下化学磷去除单元组成,作为低成本和高效的过程。为了确认在环境温度下通过微食EGSB反应器和化学磷去除过程的组合再利用国内污水处理技术的可行性,分析了微生物EGSB反应器的操作特性。此外,采用硫酸铝,PAC,三氯化铝和PE的最终化学沉淀,以增强来自微毒性EGSB系统的TP去除。研究专注于絮凝和沉降时间,凝血剂剂量,pH和温度对微生物EGSB反应器的流出物TP的影响。所得结果表明,在15-26℃下处理家用废水的微生物EGSB反应器。并且在2.5-3.1L·H〜(-1)流入流动的条件下,3.9-4.8h HRT,2.2-2.9mH〜(-1)Vup,具有影响的COD,NH_3-N,TN和TP浓度为213 -1145,26.5-72.1,31.7-81.7和3.9-16.3mg·h〜(-1),流出鳕鱼,NH_3-N,TN和TP浓度为26.3,9.9,14.0和4.7mg·l〜(-1 ),并分别由GB 18918-2002的IA,IB,IA和EI区别标准达到。随后,必须通过化学沉淀增强微食EGSB反应器流出物的TP去除。硫酸铝,PAC,三氯化铝和PES的最佳“β”(Al〜(3+):p或Fe〜(3 +):p)为1.1,6.9,3.1和2.1,同时20分别选择10,20和15min絮凝时间。连续,沉淀到20分钟,最小TP去除效率为85%,90.8%,92%和92%,可以实现,并且流出物TP在0.71,0.43,0.38和0.38mg·l〜( - 1)分别赋予除硫酸铝外的GB 18918-2002的IA区别标准。它是0.5mg·L〜(-1)TP区别标准的强制性,以调节pH值。终结,通过微氧气EGSB反应器的组合和化学磷去除过程重用的环境温度下的国内废水处理技术是可行的。

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