TY - JOUR
T1 - Combined electrocoagulation-microfiltration-membrane distillation for treatment of hydraulic fracturing produced water
AU - Jebur, Mahmood
AU - Chiao, Yu Hsuan
AU - Thomas, Kupaaikekaiao
AU - Patra, Tanmoy
AU - Cao, Yuhe
AU - Lee, Kyunghoan
AU - Gleason, Nicholas
AU - Qian, Xianghong
AU - Hu, Yunxia
AU - Malmali, Mahdi
AU - Wickramasinghe, S. Ranil
N1 - Funding Information:
Funding for this work was provided by the Arkansas Research Alliance, National Science Foundation through (a) Industry/University Cooperative Research Center for Membrane Science, Engineering and Technology, (IIP 1822101, 1913839 1930079), (b) Research Experiences for Undergraduates REU Site: From Bench to Market: Engineering Systems for High Efficiency Separations (EEC 1659653) and the University of Arkansas. The authors gratefully acknowledge the financial support from the RAPID Manufacturing Institute, a public-private partnership between the Advanced Manufacturing Office (AMO) of the US Department of Energy and the American Institute of Chemical Engineers (AIChE) under the subaward DE-EE0007888-08-08.
Funding Information:
Funding for this work was provided by the Arkansas Research Alliance , National Science Foundation through (a) Industry/University Cooperative Research Center for Membrane Science, Engineering and Technology, ( IIP 1822101 , 1913839 1930079 ), (b) Research Experiences for Undergraduates REU Site: From Bench to Market: Engineering Systems for High Efficiency Separations ( EEC 1659653 ) and the University of Arkansas . The authors gratefully acknowledge the financial support from the RAPID Manufacturing Institute , a public-private partnership between the Advanced Manufacturing Office (AMO) of the US Department of Energy and the American Institute of Chemical Engineers (AIChE) under the subaward DE-EE0007888-08-08.
Publisher Copyright:
© 2020 Elsevier B.V.
PY - 2021/3/15
Y1 - 2021/3/15
N2 - 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 - microfiltration – 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 μm 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 °C while the feed entered the module at 60 °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.
AB - 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 - microfiltration – 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 μm 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 °C while the feed entered the module at 60 °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.
KW - Carbon nanotube
KW - Direct contact membrane distillation
KW - Electrospun membrane
KW - Fouling
KW - Wastewater
UR - http://www.scopus.com/inward/record.url?scp=85097899984&partnerID=8YFLogxK
U2 - 10.1016/j.desal.2020.114886
DO - 10.1016/j.desal.2020.114886
M3 - Article
AN - SCOPUS:85097899984
SN - 0011-9164
VL - 500
JO - Desalination
JF - Desalination
M1 - 114886
ER -