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离子交换法处理线路板厂含铜废水工艺的优化

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  • 五邑大学化学与环境工程系, 广东, 江门 529020
马晓鸥(1957- ),1982 年毕业于湖南大学,高级工程 师。电话:0750-3296353,E-mail: wydxmxo@sina.com。

收稿日期: 2005-10-06

  修回日期: 2005-10-06

  网络出版日期: 2010-10-01

Optimization of the technology of treating copper-containing wastewater from printed wire board by ion exchange process

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  • Dept. of Chemistry and Environmental Engineering, Wuyi University, Jiangmen 529020, China

Received date: 2005-10-06

  Revised date: 2005-10-06

  Online published: 2010-10-01

摘要

对某线路板厂含铜废水处理装置的离子交换柱再生工艺条件进行了优化。结果表明,当再生液流量为2000L/h,再生剂质量分数为8.5%时,每次交换出的总铜量达26.1~29.0 kg;采用再生液二次利用工艺时,每次交换出的总铜量为18.5~21.3kg,废再生液Cu2+质量浓度上升到20g/L,可节约再生剂用量,并有利于铜的回收。

本文引用格式

马晓鸥, 尹庚明 . 离子交换法处理线路板厂含铜废水工艺的优化[J]. 工业水处理, 2006 , 26(2) : 81 -83 . DOI: 10.11894/1005-829x.2006年.26(02).101

Abstract

The regeneration condition of ion exchange resin has been optimized for the copper-containing wastewater device of printed wire board. The experimental results showthat the exchanged copper volume is 26.1-29.0 kg/cyc when the regeneration liquid flow rate is 2 000 L/h and the regenerant concentration is 8.5%. When the re generation liquid is used again, the total copper is exchanged to18.5-21.3 kg/cyc and Cu 2+ rise to about 20 g/L. This technology is in favor of recovering copper and saving the regenerant.

参考文献

[1] 唐受印. 废水处理工程
[M]. 北京: 化学工业出版社, 1998: 140-146.
[2] 薛明强. 离子交换树脂最适再生条件探索[J]. 苏州大学学报, 1999, 15(2): 77-80.

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