Fouling control in ultrafiltration of secondary effluent using polyaniline/TiO2 adsorption and subsequent treatment of desorption eluate using electrochemical oxidation

被引:27
作者
Li, Xiaoliang [1 ]
Tang, Gang [1 ]
Zhang, Dou [1 ]
Wu, Linjie [1 ]
Lu, Sijia [1 ]
Zhang, Yaozhong [1 ]
Cao, Xin [1 ]
Cheng, Wen [1 ]
Feng, Jiangtao [2 ]
Yan, Wei [2 ]
Pan, Baozhu [1 ]
Li, Li [1 ]
Li, Zhanbin [1 ]
Zheng, Xing [1 ]
机构
[1] Xian Univ Technol, State Key Lab Ecohydraul Northwest Arid Reg, Xian 710048, Shaanxi, Peoples R China
[2] Xi An Jiao Tong Univ, Dept Environm Sci & Engn, Xian 710049, Shaanxi, Peoples R China
基金
中国国家自然科学基金;
关键词
Secondary effluent; PANI/TiO2; adsorption; Membrane fouling; Biopolymers; Electrochemical oxidation; WASTE-WATER; ACTIVATED CARBON; AQUEOUS-SOLUTION; REMOVAL; COMPOSITE; ACID; COAGULATION; BEHAVIOR; NITRATE; MATTER;
D O I
10.1016/j.cej.2019.122915
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Performance of three adsorbents, polyaniline-modified TiO2 (PANI/TiO2), Dow resin IRA(a) and Dow resin IRA(b), in removing organics from secondary effluent (SE) was evaluated, and the objective of this study is to deliver a treatment loop including membrane fouling control using adsorption and treatment of correspondingly formed desorption eluate using electrochemical oxidation, so that the contaminants could be effectively handled within a wastewater treatment plant. Results show that PANI/TiO2 is a promising adsorbent in the removal of effluent organic matter (> 55%) and its regeneration was superior to the two others. Specifically, PANI/TiO2 could remove over 70% of the fraction of biopolymers from the SE and therefore alleviated subsequent membrane fouling to a large extent, while the other two presented less antifouling effect due to limited removal of the major foulants, though they both showed comparable effect as PANI/TiO2 in the removal of other organic fractions. BOD5/COD of the concentrated desorption eluate was gradually increasing along with the extension of the electrochemical oxidation. It reached > 0.4 after 4.5 h of treatment, which is of suitable biodegradability for recycling to the influent of the wastewater treatment plant. The improvement on BOD5/COD was due to the mineralization of effluent organic matter and simultaneous minifying of their molecular size. Moreover, the operation cost of the treatment loop was estimated at about 0.12-0.15 USD/m(3) for delivering effect fouling control and significant improvement on effluent quality.
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页数:8
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