Combined electrocoagulation-microfiltration-membrane distillation for treatment of hydraulic fracturing produced water

被引:47
作者
Jebur, Mahmood [1 ,7 ]
Chiao, Yu-Hsuan [1 ]
Thomas, Kupaaikekaiao [2 ]
Patra, Tanmoy [3 ]
Cao, Yuhe [1 ]
Lee, Kyunghoan [4 ]
Gleason, Nicholas [4 ]
Qian, Xianghong [3 ]
Hu, Yunxia [5 ]
Malmali, Mahdi [6 ]
Wickramasinghe, S. Ranil [1 ]
机构
[1] Univ Arkansas, Ralph E Martin Dept Chem Engn, Fayetteville, AR 72701 USA
[2] Univ Colorado Boulder, Chem & Biol Engn, Boulder, CO 80309 USA
[3] Univ Arkansas, Dept Biomed Engn, Fayetteville, AR 72701 USA
[4] Northwest Arkansas Community Coll, Dept Sci & Math, Bentonville, AR 72712 USA
[5] Tianjin Polytech Univ, Sch Mat Sci & Engn, Natl Ctr Int Res Membrane Sci & Technol, State Key Lab Separat Membranes & Membrane Proc, Tianjin 300387, Peoples R China
[6] Texas Tech Univ, Dept Chem Engn, Lubbock, TX 79409 USA
[7] Tikrit Univ, Dept Chem Engn, Tikrit, Salah Al Din, Iraq
基金
美国国家科学基金会;
关键词
Carbon nanotube; Direct contact membrane distillation; Electrospun membrane; Fouling; Wastewater; SHALE GAS; WASTE-WATER; ULTRAFILTRATION; NANOFILTRATION; TRANSPORT; FLOWBACK; ALUMINUM; RECOVERY; CHLORIDE; OSMOSIS;
D O I
10.1016/j.desal.2020.114886
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Hydraulic fracturing flowback and produced water is a highly impaired wastewater containing dissolved salts polar and non-polar organic compounds, oil and surfactants. Here a combined electrocoagulation micro filtration - membrane distillation process has been used to treat this wastewater. Electrocoagulation followed by microfiltration was used to pretreat the wastewater prior membrane distillation. The initial total dissolved solids (TDS) concentration was extremely high being 245,300 mg L-1. After electrocoagulation, the total organic carbon (TOC) was reduced from 120 mg L-1 to 64 mg L-1. Tangential flow microfiltration using a 0.1 mu m pore size polyethersulfone membrane was used to separate the particulate matter after electrocoagulation and to further reduce the TOC to 44 mg L-1. Membrane distillation was used to desalinate the pretreated produced water resulting in a high quality treated water (TDS of 56 mg L-1 and TOC 1 mg L-1). Three membranes with very different surface morphology were used: commercially available polyvinylidene fluoride, electrospun poly (vinylidene fluoride-co-hexafluoropropylene) nanofibers and multiwalled carbon nanotube coated polytetrafluoroethylene. The TDS in the retentate increased to over 350,000 mg L-1. During membrane distillation, the temperature of the feed tank was maintained at 36 degrees C while the feed entered the module at 60 degrees C in order to minimize scaling on the membrane. The surface properties of an ideal membrane that is resistant to wetting and provides high flux is likely to depend on the TDS and properties of the wastewater.
引用
收藏
页数:12
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