首页|矿井水的双盐流电氧化还原脱盐研究

矿井水的双盐流电氧化还原脱盐研究

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通过双盐流电氧化还原脱盐(double salt stream electroredox desalination,DSSED)系统对模拟的宁东能源化工基地煤矿矿井水进行研究.主要分析在不同电压和电解质浓度下,DSSED系统处理6 000 mg/L NaCl溶液的能耗、脱盐速率和耐久性.结果表明,DSSED系统处理6 000mg/L NaCl溶液,能耗小于0.2kW·h/m3,最高平均脱盐速率可达197.5 µg/(cm2·min),DSSED系统的稳定性与重复性良好.在最佳工作条件下,DSSED系统在4 h内可将模拟的宁东能源化工基地煤矿矿井水(ρ=6 000 mg/L)降至淡水水平(ρ<500 mg/L),平均脱盐速率达到160 µg/(cm2·min),离子的去除率均达到90%,能耗为0.397 kW·h/m3,可为宁东能源化工基地高盐水的处理提供新的解决思路.
Research on Double Salt Stream Electroredox Desalination of Mine Water
In this paper,a double salt stream electroredox desalination(DSSED)system is employed to treat simulated mine water from the Ningdong Coal Mine.Firstly,the energy consumption,salt removal rate,and durability of 6 000 mg/L NaCl saltwater treated by the DSSED under different voltages and electrolyte concen-trations are compared.The results indicate that the energy consumption of the DSSED system for treating 6 000 mg/L NaCl saltwater is less than 0.2 kW·h/m3,and the highest average salt removal rate can reach 197.5 μg/(cm2·min),demonstrating good stability and repeatability.Under the best working conditions,the DSSED system can desalinate simulated mine water from the Ningdong Coal Mine to freshwater level(<500 mg/L)within 4 hours,achieving an average salt removal rate of 160 μg/(cm2·min),an ion removal rate of 90%,and an energy consumption of 0.397 kW·h/m3.This study provides a new solution for the treatment of high-concentration saltwater in the Ningdong area.

mine water desalinationelectroredox[Fe(CN)6]3-/[Fe(CN)6]4-high concentration saltwater

武哲、明凯亮、马品、张洲洋、聂静、李海波

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宁夏大学 材料与新能源学院,宁夏 银川 750021

矿井水淡化 电氧化还原 [Fe(CN)6]3-/[Fe(CN)6]4- 高浓度盐水

2024

宁夏大学学报(自然科学版)
宁夏大学

宁夏大学学报(自然科学版)

CSTPCD
影响因子:0.377
ISSN:0253-2328
年,卷(期):2024.45(4)