4.7 Article

Sulfate and divalent cations recovery from municipal nanofiltration concentrate using two-step ion exchange membrane electrolysis

Journal

DESALINATION
Volume 541, Issue -, Pages -

Publisher

ELSEVIER
DOI: 10.1016/j.desal.2022.116055

Keywords

Electrolysis; Ion exchange membrane; Nanofiltration concentrate; Resource recovery

Funding

  1. Funds for the Central Universities
  2. National Natural Science Foundation of China [51978198]
  3. State Key Laboratory of Urban Water Resource and Environment [2020DX04]
  4. Fundamental ResearchFunds for the Central Universities

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This study recovered calcium ions, magnesium ions, and sulfate from municipal nanofiltration concentrate through a two-step ion exchange membrane electrolysis process. The process reduced the concentrations of calcium cation, magnesium cation, and sulfate anion, and also removed dissolved organic carbon.
Municipal nanofiltration (NF) concentrate generally contains sulfate and divalent cations. In this study, the SO42-, Ca2+, and Mg2+ were recovered by the two-step ion exchange membrane (IEM) electrolysis, which included anion exchange membrane (AEM) electrolysis and subsequent cation exchange membrane (CEM) electrolysis. The results showed that the AEM electrolysis recovered calcium ions and magnesium ions by forming calcium carbonate crystals and amorphous magnesium hydroxide and simultaneously concentrated the sulfate into the anode chamber; while the CEM electrolysis promoted the formation of ettringite, amorphous magnesium hydroxide, and other precipitates with the assistance of calcium hydroxide and sodium metaaluminate, thereby recovering the sulfate and divalent cations in the NF concentrate. The calcium cation, magnesium cation, and sulfate anion concentrations were reduced by 80.0 %, 93.3 %, and 43.1 %, respectively. In addition, the dissolved organic carbon was removed by 31.0 % through the two-step membrane electrolysis. The AEM fouling was much greater than that of the CEM. The total energy consumption of the two-step IEM electrolysis process was calculated as 4.3-6.7 kWh/m(3). These findings provide practical relevance for the advanced treatment of municipal NF concentrate.

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