淡水室填充阳离子交换树脂的EDI膜堆对镍离子溶液分离性能的研究 |
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引用本文: | 牛玉标,徐小青,赵海洋,周志军.淡水室填充阳离子交换树脂的EDI膜堆对镍离子溶液分离性能的研究[J].中国工程科学,2014,16(7):62-67. |
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作者姓名: | 牛玉标 徐小青 赵海洋 周志军 |
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作者单位: | 浙江大学膜与水处理技术教育部工程研究中心,杭州310027;浙江大学膜与水处理技术教育部工程研究中心,杭州310027;浙江大学膜与水处理技术教育部工程研究中心,杭州310027;浙江大学膜与水处理技术教育部工程研究中心,杭州310027 |
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基金项目: | 科技部科技型中小企业技术创新基金(12C26213302815) |
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摘 要: | 采用淡水室填充阳离子交换树脂的电去离子(EDI)膜堆来处理低浓度含镍废水,考察了该EDI膜堆用于低浓度重金属废水处理的可行性,并探讨了膜堆电压和料液流量对EDI分离重金属离子性能的影响。结果表明,对于Ni2+浓度为50 mg/L,pH为4.5的料液工况,操作电压为25 V,料液处理量为20 L/h时,可保证淡水产水Ni2+浓度在2 mg/L以下,且浓缩水Ni2+浓度大于900 mg/L,电流效率达到24.2%。
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关 键 词: | EDI 阳离子交换树脂 重金属 镍离子 |
收稿时间: | 5/7/2014 12:00:00 AM |
修稿时间: | 2014/5/15 0:00:00 |
Study on the performance of EDI device in dealing with Ni2 solution with dilute departments filled with cation exchange resins |
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Abstract: | Study on the feasibility of EDI device, whose dilute departments were filled with cation exchange resins and feed water was low concentration Ni2 solution, for the treatment of low-concentration heavy-metal wastewater. The effects of operating voltage and dilute flow flux on the separation performances EDI processes were investigated. With the feed solution whose Ni2 concentration was 50 mg?L-1 and pH was 4.5, the results show that the out dilute Ni2 concentration was lower than 2 mg.L-1 and the Ni2 concentration of out concentrate could higher than 900 mg.L-1 when operating voltage was 25 v and dilute flow flux was 20 L.h-1. |
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Keywords: | Electrodeionization (EDI) cation exchange resin heavy-metal Ni2 |
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