The elimination of turbidity and organochlorine (OCPs) in high-turbidity water by enhanced coagulation was studied. A composite coagulant was prepared by Poly Aluminium Chloride (PAC) and Poly Dimethyl Diallyl Propy Ammoniuml Chloride (PDMDAAC). The effect of PAC-PDMDAAC composite ratio, dosage of the composite coagulant, initial turbidity, the time for slow stirring and pH on the elimination efficiencies of turbidity and OCPs were tested and characterized by fractal dimension of flocs and Zeta potentials to verify the result. The results show that PAC-PDMDAAC ratio has great influence on the removal effect of OCPs and turbidity. The removal rates of turbidity and OCPs reach the highest values when the PAC-PDMDAAC composite ratio is 5:1, the dosage of PAC-PDMDAAC is 1ml/L, and the time for slow stirring is 15min. With the increase of initial turbidity, the removal rate of OCPs in the water is also increased which shows that the PAC-PDMDAAC apply to high turbidity water. Compared with other coagulants, The PAC-PDMDAAC composite coagulant has wide pH range suitable for use, the removal rates of turbidity and OCPs reach the best when the pH is 4. The coagulation effects are well verified and explained by measuring the fractal dimension of flocs and Zeta potential of particles.
贺建栋, 刘鹏宇, 常青, 张翠玲. PAC与PDMDAAC复合混凝剂去除高浊度水中有机氯[J]. 中国环境科学, 2016, 36(6): 1738-1745.
HE Jian-dong, LIU Peng-yu, CHANG Qing, ZHANG Cui-ling. Efficiency of the PAC-PDMDAAC composite coagulant for eliminating the organochlorines in high-turbidity water. CHINA ENVIRONMENTAL SCIENCECE, 2016, 36(6): 1738-1745.
Xuewei H, Aimin L, Conglin D ,et al. Treatment of nitrobenzene was tewater containing high salinity through combining res in adsorption and bio-intens ifying [J]. Industrial Water Treatment, 2007,27(12):40-42.
[7]
Xin Z, Lingling B, Jiajia H, et al. Treatment of pH armaceutical wastewater by CaO flocculation sedimentation and resin adsorption [J]. Chemical Industry and Engineering Progress, 2011(3):671-674.
[8]
Cao J S, Zhang W X, Brown D G,et al. Oxidation of lindane with Fe(II)-activated sodium persulfate [J]. Environmental Engineering Science, 2008,25(2):221-228.
[9]
Elliott D W, Spear S T, Zhang W X. Novel products from the degradation of lindane by nanoscale zero valent iron [J]. Abstracts of Papers of the American Chemical Society, 2005,229:935-936.
Hong Hl B G. Residual marrow effect of lindane in mice following irradiation [J]. Faseb Journal, 1991,5(4):485.
[12]
G K, Ms B. Oxidation of lindane in contaminated water under solar irradiation in the presence of photo catalyst and oxidizing agents [J]. Bulgarian Chemical Communications, 2010,42(2):161-166.
[13]
Mohamed K A, Basfar A A, Al-Kahtani H A, et al. Radiolytic degradation of malathion and lindane in aqueous solutions [J]. Radiation PHysics and Chemistry, 2009,78(11):994-1000.
[14]
戴之荷.受污染高浊度水净化新技术 [J]. 给水排水, 2001, 27(3):2-8.
[15]
Tang H X, Luan Z K, Wang D S, et al. Composite in organic polymer flocculants [A]. Chemical Water and Wastewater Treatment V [M]. Berlin: Czech Republic, Springer Press, 1998,25-34.
GilG, Patrick W, Matthew M. Enhanced coagulation: Its effect on NOM removal and chemical costs [J]. JAW-WA. 1995,87(1):78-89.
[18]
Moussas P A, Zouboulis A I. A new inorganic-organic composite coagulant, Consisting of polyferric sulpHate (PFS) and polyacrtlamide (PAA) [J]. Water Res, 2009,43(14):3511-3524.
Clifford P J, LI X Y, Logan B E. Settling velocities of fractal aggregates [J]. Environ. Sci. Tech., 1996,30:1911-1981.
[36]
Da H L, Jerzy G. Fractal geometry of particle aggregates generated in water and wastewater treatment processes [J]. Environ Sci Tech, 1989,23:1385-1390.
[37]
Waite T D. Measurement and implications of floc structure in water and wastewater treatment [J]. Colloids and Surfaces A:Physicochemical and Engineering Aspects, 1999(5):27-41.
Henderson R K, Parsons S A, Jefferson B. Successful removal of algae through the control of Zeta potential [J]. Separation Science and Technology, 2008,43:1653-1666.
[41]
Liu Hui-jun. Study of ζ potential as index of coagulants treatment capacity [J]. Technology of Water Treatment, 2002,28(2):78-81.