2023
DOI: 10.1039/d2ew00924b
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Treatment of brackish water inland desalination brine via antiscalant removal using persulfate photolysis

Abstract: Brine disposal is a challenging issue for brackish water desalination in inland regions. This study developed an ultraviolet-driven persulfate oxidation pre-treatment (UV/PS) followed by a chemical demineralization (CDM) and microfiltration...

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Cited by 4 publications
(7 citation statements)
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“…6 Consequently, the further concentration of ROC remains challenging due to the membrane fouling/scaling induced by a high concentration of retentates coupled with a diverse mix of substances present in ROC. 7 Currently, the concentration technology for ROC mainly includes thermal concentration and membrane concentration. Thermal-based concentration technologies are relatively energy-intensive.…”
Section: Introductionmentioning
confidence: 99%
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“…6 Consequently, the further concentration of ROC remains challenging due to the membrane fouling/scaling induced by a high concentration of retentates coupled with a diverse mix of substances present in ROC. 7 Currently, the concentration technology for ROC mainly includes thermal concentration and membrane concentration. Thermal-based concentration technologies are relatively energy-intensive.…”
Section: Introductionmentioning
confidence: 99%
“…6 Consequently, the further concentration of ROC remains challenging due to the membrane fouling/scaling induced by a high concentration of retentates coupled with a diverse mix of substances present in ROC. 7…”
Section: Introductionmentioning
confidence: 99%
“…Hence, a scale inhibitor is necessary before SRO to avoid mineral salt scaling on the surface of the SRO membrane [16][17][18]. After SRO, the scale inhibitors in the SRO concentrate need to be destroyed to precipitate CaSO 4 [17,19]. Accordingly, we propose the following two-stage inhibitor is necessary before SRO to avoid mineral salt scaling on the surface of the SRO membrane [16][17][18].…”
Section: Introductionmentioning
confidence: 99%
“…Accordingly, we propose the following two-stage inhibitor is necessary before SRO to avoid mineral salt scaling on the surface of the SRO membrane [16][17][18]. After SRO, the scale inhibitors in the SRO concentrate need to be destroyed to precipitate CaSO4 [17,19]. Accordingly, we propose the following two-stage RO process with ICD to treat brines (Figure 1), where the SRO concentrate is treated with ICD to remove CaSO4 and then mixed with the PRO concentrate for further desalination in SRO.…”
Section: Introductionmentioning
confidence: 99%
“…[1][2][3] Moreover, there is a severe shortage of drinking water resources in the world. 4,5 Hence, the supply of freshwater using salt water desalination or wastewater treatment is very necessary and vital. Traditional freshwater production methods, such as reverse osmosis, [6][7][8] multi-stage ash distillation, 9 multi-effect distillation, 10 electrodialysis/electrodialysis reversal, 11 membrane distillation, 12,13 and capacitive deionization 14,15 are facing three key challenges: complex equipment requirements, high energy consumption, and high cost.…”
Section: Introductionmentioning
confidence: 99%