Integrated membrane process of tubular ultrafiltration-nanofiltration-electrodialysis-reverse osmosis for treating fracturing flowback fluid

被引:0
|
作者
Xu, Bing [1 ]
Zhang, Qian [1 ]
Wu, Huanhuan [1 ]
Tian, Qianqian [1 ]
Chai, Wenming [2 ]
Zhang, Ming [2 ]
Shao, Guangyi [1 ]
Tian, Shuwen [1 ]
Lin, Yakai [3 ]
Yao, Hong [1 ]
机构
[1] Beijing Jiaotong Univ, Engn Res Ctr Clean & Low carbon Technol Intelligen, Beijing Key Lab Aqueous Typ Pollutants Control & W, Sch Environm,Minist Educ,Beijing Int Sci & Technol, Beijing 100044, Peoples R China
[2] Inner Mongolia Lilong Water Co LTD, Ordos 017000, Peoples R China
[3] Tsinghua Univ, Dept Chem Engn, Beijing Key Lab Membrane Mat & Engn, Beijing 100084, Peoples R China
基金
中国国家自然科学基金;
关键词
Fracturing flowback fluid; Membrane integrated process; Tubular ultrafiltration; Nanofiltration; Electrodialysis; WASTEWATERS; SEPARATION;
D O I
10.1016/j.jclepro.2024.142995
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
As an underground source of natural gas, shale gas is important for ensuring national energy security and promoting the "dual carbon" target. However, shale gas extraction produces flowback fluid that requires efficient treatment to avoid negative impacts on the environment and human health. In this study, a pilot plant was constructed to implement a novel membrane-integrated process to treat fracturing flowback fluid. This process employs an aeration reaction sedimentation (ARS) tank and a tubular ultrafiltration (TUF) membrane for pretreatment, followed by three separate membranes for nanofiltration (NF), electrodialysis (ED), and reverse osmosis (RO). The pretreatment removed 99.3% of total hardness, 99.4% of total suspended solids (TSS), and 88.1% of total organic carbon (TOC). Four different types of TUF membranes were tested and compared. It was also found that physico-chemical cleaning of the TUF membrane using the ceramic particle technology resulted in a flux recovery rate of up to 98%. In addition, the NF and ED membranes can remove 99.4% of Na2SO4 2 SO 4 and 90% of NaCl, respectively, resulting in an 85.6% decrease in TSS. Water recovery rate of the total system can reach 90%. Based on concept of sustainable green development, carbon footprint of integrated membrane process for treating fracturing flowback fluid was approximately 86.7 kgCO2 2 eq lower than that of traditional process. Low carbon emissions and no generation of secondary pollutants have become the keys to treat fracturing wastewater. In summary, the integrated TUF-NF-ED-RO process based on membranes is very promising for treating fracturing flowback fluid.
引用
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页数:10
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