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水处理除盐系统出力不足的原因分析及处理措施

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  • 1. 河南电力试验研究所, 河南郑州 450052;
    2. 郑州热电厂, 河南郑州 450052
王锋涛(1976- ),1998年毕业于东北电力学院应用化学系,助理工程师.电话:0371-7906357,E-mail:wftwyx@371.net.

收稿日期: 2001-02-14

  网络出版日期: 2010-10-01

Cause analyses and handling measures of the insufficient output in the desalination system by water treatment

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  • 1. Henan Electric Power Research Institute, Zhengzhou 450052, China;
    2. Zhengzhou Heating Power Plant, Zhengzhou 450052, China

Received date: 2001-02-14

  Online published: 2010-10-01

摘要

针对郑州热电厂五期补给水处理一级除盐系统酸碱耗大、自用水率高、出力严重不足等问题,对现场进行了调查研究,分析了主要原因,并提出了相应的处理措施,最终使问题得以解决。

本文引用格式

王锋涛, 张春雷, 赵战省, 王克涛, 李献敏, 张莉 . 水处理除盐系统出力不足的原因分析及处理措施[J]. 工业水处理, 2001 , 21(8) : 40 -42 . DOI: 10.11894/1005-829x.2001.21(8).40

Abstract

Aiming at the problems such as the large acid and alkali consumption, high self-using water ratio and seriously insufficient output in the first step desalination system of the Zhengzhou Heating Power Plant.Investigations have been made in situ.The main causes have been made analysed,handling measures have been presented and the problems have finally been solved.

参考文献

[1] 邵林.强碱性阴离子交换树脂的交换特性,水处理用离子交换树脂[M].北京:水利电力出版社,1989:229~235.
[2] 姚继贤,等.离子交换树脂的污染和复苏,工业锅炉水处理及水质分析[M].北京:中国劳动出版社,1993:187~195.

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