2019
DOI: 10.1016/j.scitotenv.2019.06.539
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Eco-efficient treatment of ion exchange spent brine via electrodialysis to recover NaCl and minimize waste disposal

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Cited by 23 publications
(20 citation statements)
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“…Indeed, due to the disappearance of the boundary layer and the regular re-homogenization of the solution around the membranes, the PEFs have proven to be an effective solution to mitigate fouling caused by humate [ 39 , 102 ], proteins [ 103 , 104 ], peptides/amino acids [ 105 ], lignin [ 106 ], natural organic matter [ 107 ], partially hydrolyzed polyacrylamid [ 84 ] and mineral scaling [ 64 , 65 , 83 , 84 , 85 , 104 , 108 , 109 , 110 , 111 , 112 , 113 ] during electrodialytic processes ( Table 1 ). Deep investigations have been carried out to reveal the mechanisms of scaling prevention under the action of PEF [ 104 , 109 , 110 , 114 ] as well as fouling mitigation by natural organic matter [ 107 , 115 , 116 , 117 ] and lignin [ 106 ]. Regarding specific migration of mineral ions, the difference in monovalent and divalent ion demineralization caused by PEF could be explained by several points reported in the literature.…”
Section: Membrane Phenomenamentioning
confidence: 99%
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“…Indeed, due to the disappearance of the boundary layer and the regular re-homogenization of the solution around the membranes, the PEFs have proven to be an effective solution to mitigate fouling caused by humate [ 39 , 102 ], proteins [ 103 , 104 ], peptides/amino acids [ 105 ], lignin [ 106 ], natural organic matter [ 107 ], partially hydrolyzed polyacrylamid [ 84 ] and mineral scaling [ 64 , 65 , 83 , 84 , 85 , 104 , 108 , 109 , 110 , 111 , 112 , 113 ] during electrodialytic processes ( Table 1 ). Deep investigations have been carried out to reveal the mechanisms of scaling prevention under the action of PEF [ 104 , 109 , 110 , 114 ] as well as fouling mitigation by natural organic matter [ 107 , 115 , 116 , 117 ] and lignin [ 106 ]. Regarding specific migration of mineral ions, the difference in monovalent and divalent ion demineralization caused by PEF could be explained by several points reported in the literature.…”
Section: Membrane Phenomenamentioning
confidence: 99%
“…When natural organic matter (NOM) is removed by ion-exchange (IX) via anionic IX resin from potable water for aesthetic, operational and indirect health concerns, it generates spent brine. To overpass this main drawback related to the strict discharge regulations and limited and costly brine management options, ED-PEF desalination of the IX brine was tested recently [ 107 ]. The highest demineralization rate (95.5%) was achieved when the IX spent brine was treated under the PEF regime with conventional permselective AEMs instead of monovalent permselective AEMs (AMX vs. ACS) and the PEF regime was efficient in intensifying the desalination process only when the conventional AEMs were used.…”
Section: Recent Technological Developments Based On Ed Membrane Phmentioning
confidence: 99%
“…The potential reuse of the NOM solution should be further studied, since its quality was impaired by heavy metals. A simpler process was adopted for an IX spent brine with NaCl, sulphate and NOM concentrations of 90, 1, and 1 g/L (as dissolved organic carbon), respectively [522]. A single ED step (spent brine as diluate, 2 g/L NaCl solution as concentrate) with MVMs was effective, yielding a pure NaCl solution with 88.8% removal, negligible membrane fouling, and E spec of 2 kWh/kg salt.…”
Section: Spent Brinementioning
confidence: 99%
“…Several methods to conventionally dispose of the AIX spent brine, such as discharge after dilution, deep well injection, landfill, discharge in the sewer or other surface water bodies, sea and ground storage, and evaporation pounds, have been investigated [ 7 , 8 , 9 ]. However, these methods either cause secondary pollution such as severe groundwater, surface water, soil and sea contamination, causing the destruction of marine ecological balance and soil salinization [ 3 , 4 , 10 ], or high energy consumption and operation costs [ 11 ].…”
Section: Introductionmentioning
confidence: 99%
“…Nevertheless, the recovered NaCl solution concentration cannot meet the concentration requirement as a saturated resin regeneration agent, and resource reuse of recovered NaCl and NOM was not investigated. Additionally, desalination performance of ion exchange spent brine via ED, about applied electric field and the ion exchange membrane permselectivity impact, was discussed [ 11 ]. However, the practical application of the recovered NaCl solutions and transport of organic matters during the ED process were not systematically evaluated.…”
Section: Introductionmentioning
confidence: 99%