TY - JOUR
T1 - Increasing water recovery during reclamation of treated municipal wastewater using bipolar membrane electrodialysis and fluidized bed crystallization
AU - AzadiAghdam, Mojtaba
AU - Achilli, Andrea
AU - Snyder, Shane A
AU - Farrell, James
N1 - Funding Information:
Authors thank the United States National Science Foundation ( PFI: AIR-TT: 1640445 ) for providing the funding for this work. We also acknowledge Mr. Shawn Beitel from University of Arizona for facilitating the use of the instruments, Agilent Technologies for their continued technical and equipment support to the Snyder Research Lab, and Dow Chemical Company and EconoPure LLC for their equipment support. Funding sources had no role in the research activities or in the preparation of this manuscript.
Funding Information:
Authors thank the United States National Science Foundation (PFI: AIR-TT: 1640445) for providing the funding for this work. We also acknowledge Mr. Shawn Beitel from University of Arizona for facilitating the use of the instruments, Agilent Technologies for their continued technical and equipment support to the Snyder Research Lab, and Dow Chemical Company and EconoPure LLC for their equipment support. Funding sources had no role in the research activities or in the preparation of this manuscript.
Publisher Copyright:
© 2020 Elsevier Ltd
PY - 2020/12
Y1 - 2020/12
N2 - This research investigated the effectiveness of bipolar membrane electrodialysis coupled with fluidized bed crystallization and coagulation/flocculation with FeCl3 for removing potential membrane foulants from reverse osmosis (RO) concentrate solutions produced during reclamation of municipally treated wastewater. The goal of the treatment process was to produce water with low concentrations of potential foulants that could be subjected to a high recovery secondary RO process. Effluent from the secondary clarifier at a municipal wastewater treatment plant was treated by ultrafiltration and RO at a recovery of 60–65 %. The RO concentrate solution was then fed into a fluidized bed crystallization reactor operating at a pH value of 11.5. Calcium, magnesium, silica and dissolved organic matter were removed from the RO concentrate via precipitation of mineral solids on 60 mesh garnet sand. The acid and base utilized in the fluidized bed crystallization reactor was produced using bipolar membrane electrodialysis from the treated RO concentrate solution after polishing with coagulation/flocculation with FeCl3. The treatment system was able to remove 84 % of Ca2+, 93 % of Ba2+, >99 % of Mg2+, 80 % of total organic carbon (TOC), and 68 % of dissolved silica from the RO concentrate solutions. The product water produced by the system contained mostly Na+, Cl− and SO42- ions, with ≤ 10 mg/L Ca2+ and SiO2, ≤ 2 mg/L TOC, and ≤ 1 mg/L Mg2+. The electrical energy for operating the bipolar membrane electrodialysis cell amounted to 110 kW h per kmol of acid and base produced, which translates to 3.5 kW h/m3 of treated RO concentrate.
AB - This research investigated the effectiveness of bipolar membrane electrodialysis coupled with fluidized bed crystallization and coagulation/flocculation with FeCl3 for removing potential membrane foulants from reverse osmosis (RO) concentrate solutions produced during reclamation of municipally treated wastewater. The goal of the treatment process was to produce water with low concentrations of potential foulants that could be subjected to a high recovery secondary RO process. Effluent from the secondary clarifier at a municipal wastewater treatment plant was treated by ultrafiltration and RO at a recovery of 60–65 %. The RO concentrate solution was then fed into a fluidized bed crystallization reactor operating at a pH value of 11.5. Calcium, magnesium, silica and dissolved organic matter were removed from the RO concentrate via precipitation of mineral solids on 60 mesh garnet sand. The acid and base utilized in the fluidized bed crystallization reactor was produced using bipolar membrane electrodialysis from the treated RO concentrate solution after polishing with coagulation/flocculation with FeCl3. The treatment system was able to remove 84 % of Ca2+, 93 % of Ba2+, >99 % of Mg2+, 80 % of total organic carbon (TOC), and 68 % of dissolved silica from the RO concentrate solutions. The product water produced by the system contained mostly Na+, Cl− and SO42- ions, with ≤ 10 mg/L Ca2+ and SiO2, ≤ 2 mg/L TOC, and ≤ 1 mg/L Mg2+. The electrical energy for operating the bipolar membrane electrodialysis cell amounted to 110 kW h per kmol of acid and base produced, which translates to 3.5 kW h/m3 of treated RO concentrate.
KW - Bipolar membrane electrodialysis
KW - EEM spectra
KW - NOM removal
KW - RO concentrate
KW - Water reclamation
UR - http://www.scopus.com/inward/record.url?scp=85089244731&partnerID=8YFLogxK
UR - http://www.scopus.com/inward/citedby.url?scp=85089244731&partnerID=8YFLogxK
U2 - 10.1016/j.jwpe.2020.101555
DO - 10.1016/j.jwpe.2020.101555
M3 - Article
AN - SCOPUS:85089244731
SN - 2214-7144
VL - 38
JO - Journal of Water Process Engineering
JF - Journal of Water Process Engineering
M1 - 101555
ER -