Department of Process Engineering, Faculty of Technology, University of Saàd Dahlab Blida 1, P.O. Box 270, 09000, Blida, Algeria; National Centre for Research and Development of Fisheries and Aquaculture (CNRDPA) 11, Bd Amirouche P.O. Box 67, Bousmail, W. Tipaza, Algeria.
Department of Process Engineering, Faculty of Technology, University of Saàd Dahlab Blida 1, P.O. Box 270, 09000, Blida, Algeria; National Centre for Research and Development of Fisheries and Aquaculture (CNRDPA) 11, Bd Amirouche P.O. Box 67, Bousmail, W. Tipaza, Algeria; Laboratory of Natural Substances Chemistry and Biomolecules, University of Saàd Dahlab Blida 1, P.O. Box 270, 09000, Blida, Algeria.
J Environ Manage. 2018 Nov 15;226:106-119. doi: 10.1016/j.jenvman.2018.08.038. Epub 2018 Aug 14.
The present work undertakes an examination and comparison of electro-Fenton (EF), electro-peroxi-coagulation (EPC) and electrocoagulation (EC) applied to the E. coli inactivation in batch reactor. Indeed, platinum (Pt (anode), EF), stainless steel (SS (cathode), EF, EPC) and ordinary steel (Fe (anode), EPC) and aluminum (Al, EC) were used respectively. The current intensity, nature of electrolytic support, bacterial density and hydrogen peroxide (HO) concentration are the most influenced study parameters. The obtained results showed that the high current intensities were significant for better inactivation and destruction of E. coli cells and caused a maximum of energy consumption. Both disinfection and energy consumption were improved by adding NaCl (or NaSO) in the three processes. Higher cellular density limited the electrochemical process and has negative effect in E. coli inactivation and the energy consumption. Only in the EPC case, the disinfection was considerably increased in function with HO concentration. The modeling parameters of the inactivation kinetics of E. coli showed a good fitting of the established model (0.9560 < R < 0.9979, 0.9267 < R adjusted <0.997 and 0.0189 < RMSE <0.4821), faster kinetics of E. coli inactivation (significant values of K and Sl) in the case of high current intensity (0.2442<K<0.7440 and 10.50 < Sl < 24.69), the presence of chlorides or sulfates (0.6662<K<0.7818 and 11.67 < Sl < 18.59), and the sufficient HO concentration (0.4712<K<0.9204 and 13.00 < Sl < 16.38). Moreover, the analysis of the results revealed that the EF is more effective in terms of the E. coli inactivation and the energy consumption comparatively to the other studied processes.
本工作对电芬顿(EF)、电过氧协同混凝(EPC)和电混凝(EC)在分批式反应器中应用于大肠杆菌灭活进行了考察和比较。分别使用了铂(阳极,EF)、不锈钢(阴极,EF、EPC)和普通钢(阳极,EPC)以及铝(Al,EC)作为电解支撑物。电流强度、电解支撑物的性质、细菌密度和过氧化氢(HO)浓度是影响最大的研究参数。实验结果表明,高电流强度对于更好地灭活和破坏大肠杆菌细胞是非常重要的,并且会导致最大的能量消耗。在这三种工艺中添加 NaCl(或 NaSO)都可以提高消毒效果和能量消耗。较高的细胞密度限制了电化学过程,对大肠杆菌的灭活和能量消耗产生负面影响。只有在 EPC 情况下,HO 浓度的增加才能显著提高消毒效果。大肠杆菌灭活动力学的模型参数表明,所建立的模型拟合度较好(0.9560< R <0.9979,0.9267< R 调整值<0.997,0.0189< RMSE<0.4821),在高电流强度(0.2442< K <0.7440,10.50< Sl<24.69)、存在氯化物或硫酸盐(0.6662< K <0.7818,11.67< Sl<18.59)和足够的 HO 浓度(0.4712< K <0.9204,13.00< Sl<16.38)时,大肠杆菌的灭活动力学更快。此外,结果分析表明,与其他研究工艺相比,EF 在大肠杆菌灭活和能量消耗方面更为有效。