环境英文翻译In this paper, an improved configuration of the membrane stack was adopted in the electrodeionization (EDI) cell to prevent precipitation ofbivalent metal hydroxide during the running. The operational parameters that influenced the

环境英文翻译In this paper, an improved configuration of the membrane stack was adopted in the electrodeionization (EDI) cell to prevent precipitation ofbivalent metal hydroxide during the running. The operational parameters that influenced the
环境英文翻译
In this paper, an improved configuration of the membrane stack was adopted in the electrodeionization (EDI) cell to prevent precipitation of
bivalent metal hydroxide during the running. The operational parameters that influenced the electro-regeneration of cation exchange resins loaded
with nickel ions were optimized, and the result showed that addition of a small amount of Na2SO4 into the electrode solution, moderate increase
of applied voltage and initial metal ion concentration could get better regeneration effect. A steady and continuous process of electroplating
wastewater treatment could be achieved with current efficiency of 33–38%, removal efficiency of at least 99.8% and enrichment factor of 22–36.
Concentration of metal ions in purified water was 0.03–0.09 mg/L for nickel, 0.07–0.10 mg/L for copper, 0.06–0.15 mg/L for zinc, 0.07–0.10 mg/L
for cadmium and 0.08–0.17 mg/L for chromium, respectively. This demonstrated the applicability of recovering heavy metals and purified water
from electroplating effluent for industrial reuse.
© 2007 Elsevier B.V. All rights reserved.

环境英文翻译In this paper, an improved configuration of the membrane stack was adopted in the electrodeionization (EDI) cell to prevent precipitation ofbivalent metal hydroxide during the running. The operational parameters that influenced the
在本文,膜堆的一种被改进的配置在electrodeionization (EDI)细胞被采取防止降雨雪
在赛跑期间的二价金属氢氧化. 影响被装载的阳离子交换树脂电镀物品再生的操作的参量
镍离子被优选了,并且结果显示了少量的Na2SO4的那加法入电极解答,适度增量
应用的电压和最初的金属离子集中能得到更好的再生作用. 电镀的一个平稳和连续过程
废水处理能达到与当前效率33¨C38%,撤除效率至少99.8%和22¨C36增补因素.
金属离子的集中在被净化的水中是0.03¨C0.09镍的mg/L, 0.07¨C0.10铜的mg/L, 0.06¨C0.15锌的mg/L, 0.07¨C0.10 mg/L
为铬的镉和0.08¨C0.17 mg/L,分别. 这展示了恢复重金属的适用性并且净化了水
从工业再用的电镀的流出物.
© 2007年Elsevier B.V. 版权所有.

在这方面的文件，提出了一种改进的配置膜栈获得通过，在电去离子（ EDI ）细胞，以防止沉淀
二价金属氢氧化物在运行。操作参数影响电再生阳离子交换树脂装
与镍离子进行了优化，结果表明，加入少量的硫酸钠到电极的解决办法，适度增加
应用电压和初始金属离子浓度可以得到更好的再生效果。一个稳定和持续的过程，电镀
废水处理可达到与电流效率的33-38 ％ ，去除效率至少为99....

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在这方面的文件，提出了一种改进的配置膜栈获得通过，在电去离子（ EDI ）细胞，以防止沉淀
二价金属氢氧化物在运行。操作参数影响电再生阳离子交换树脂装
与镍离子进行了优化，结果表明，加入少量的硫酸钠到电极的解决办法，适度增加
应用电压和初始金属离子浓度可以得到更好的再生效果。一个稳定和持续的过程，电镀
废水处理可达到与电流效率的33-38 ％ ，去除效率至少为99.8 ％和富集因子22-36 。
浓度金属离子的纯净水是0.03-0.09毫克/升，为镍， 0.07-0.10毫克/升铜， 0.06-0.15毫克/升，锌， 0.07-0.10毫克/升
为镉和0.08-0.17毫克/升，为铬，分别。这表明适用于回收重金属和纯净水
从电镀废水的工业循环再用。
© 2007 Elsevier公司乙诉，保留所有权利。

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