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Desalination of concentrated wastewater from reverse osmosis by bipolar membrane electrodialysis

机译:双极膜电渗析法反渗透浓缩废水的脱盐

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The present study focused on the feasibility of bipolar membrane electrodialysis (BMED) for desalination of concentrated wastewater from reverse osmosis, including the reduction of total dissolved solids (TDS) and the generation of mixed acid/base. The effects of parameters such as current density, electrolyte concentration, and initial acid/base concentration were explored and discussed. The optimal current density was 10 mA/cm(2), the suitable electrolyte concentration was 0.25 mol/L, and the appropriate initial acid/base concentration was 0.05 mol/L. Experimental results indicated that 89.05% TDS could be removed, and the generated acid and base concentrations could reach to 0.12 mol/L and 0.18 mol/L respectively. The energy consumption for removing per kilogram TDS was 2.33 kWh. Besides, the energy consumption for acid generation was 2.55 kWh/kg, with a current efficiency of 67.7%; and for base production was 1.80 kWh/kg, with a current efficiency of 87.5%. All the results indicated that the BMED process was technical and environmental feasible for desalination of concentrated wastewater from RO. The generated mixed acid/base solution and fresh water (TDS less than 1.45 g/L) after treatment could be reused as resource.
机译:本研究集中于双极膜电渗析(BMED)用于反渗透浓缩废水脱盐的可行性,包括减少总溶解固体(TDS)和生成混合酸/碱。探索和讨论了诸如电流密度,电解质浓度和初始酸/碱浓度等参数的影响。最佳电流密度为10 mA / cm(2),合适的电解质浓度为0.25 mol / L,合适的初始酸/碱浓度为0.05 mol / L。实验结果表明,可去除89.05%的TDS,所产生的酸和碱浓度分别达到0.12 mol / L和0.18 mol / L。每千克TDS去除的能耗为2.33千瓦时。此外,制酸能耗为2.55 kWh / kg,电流效率为67.7%;基本产量为1.80 kWh / kg,电流效率为87.5%。所有结果表明,BMED工艺对于RO浓缩废水的脱盐具有技术和环境可行性。处理后产生的混合酸/碱溶液和淡水(TDS小于1.45 g / L)可作为资源重复使用。

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