Reuse of shale gas flowback and produced water: Effects of coagulation and adsorption on ultrafiltration, reverse osmosis combined process

被引:60
作者
Shang, Wei [1 ]
Tiraferri, Alberto [2 ]
He, Qiping [3 ]
Li, Naiwen [4 ]
Chang, Haiqing [1 ]
Liu, Chao [4 ]
Liu, Baicang [1 ]
机构
[1] Sichuan Univ, Inst New Energy & Low Carbon Technol, Inst Disaster Management & Reconstruct, Coll Architecture & Environm, Chengdu 610207, Sichuan, Peoples R China
[2] Politecn Torino, Dept Environm Land & Infrastruct Engn, Corso Duca Abruzzi 24, I-10129 Turin, Italy
[3] Chinese Natl Petr Corp, Chuanqing Drilling Engn Co Ltd, Chengdu 610081, Sichuan, Peoples R China
[4] Sichuan Univ, State Key Lab Hydraul & Mt River Engn, Coll Water Resource & Hydropower, Chengdu 610065, Sichuan, Peoples R China
基金
中国国家自然科学基金; 中国博士后科学基金;
关键词
Flowback and produced water; Adsorption; Coagulation; Ultrafiltration; Reverse osmosis; Water quality; ACTIVATED CARBON; ORGANIC-COMPOUNDS; WASTE-WATER; DESALINATION; REMOVAL; PAC; TECHNOLOGIES; WASTEWATERS; FUTURE; FLUID;
D O I
10.1016/j.scitotenv.2019.06.365
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The shale gas flowback and produced water (FPW) from hydraulic fracturing in the Sichuan province of China has relatively low to moderate levels of total dissolved solids (<20 g/L) and organics (<50 mg/L of dissolved organic carbon). As such, a combined ultrafiltration (UF), reverse osmosis (RO) system can be successfully applied to desalinate this feed water with the goal of reuse. However, the concentration of influent organic matter and particulates in the UF and RO stage is high, and the overall ionic and organics composition is highly complex, so that the membrane processes do not perform well, also due to fouling. To ensure the long-term and efficient operation of the UF-RO stages, a combined pretreatment of the FPW with coagulation and adsorption was investigated. The effect of different parameters on the performance on the system was studied in detail. Overall, the coagulation-adsorption pre-treatment greatly reduced fouling of the membrane processes, thanks to the high removal rate of turbidity (98.8%) and dissolved organic carbon (86.3%). The adsorption of organic matter by powdered activated carbon was best described by the Freundlich equilibrium model, with a pseudo second-order model representing the adsorption kinetics. Also, the various ions had competitive removal rates during the adsorption step, a phenomenon reported for the first time for FPW treatment. Also, an optimal dose of activated carbon existed to maximize fouling reduction and effluent quality. The overall treatment system produced a high-quality water streams, suitable for reuse. (C) 2019 Elsevier B.V. All rights reserved.
引用
收藏
页码:47 / 56
页数:10
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