CALCULATION IN WATER TREATMENT DEAIGN FOR JOINTLY USING STRONG AND WEAK ACIDIC CATION EXCHANGE RESIONS

doi:10.19666/j.rlfd.2003.03.009

English

您当前的位置：

首页 >

文章列表页 >

CALCULATION IN WATER TREATMENT DEAIGN FOR JOINTLY USING STRONG AND WEAK ACIDIC CATION EXCHANGE RESIONS

Thermal Power Generation Issue 3, Pages: 29-32(2003)

更新时间：2025-09-28

- CALCULATION IN WATER TREATMENT DEAIGN FOR JOINTLY USING STRONG AND WEAK ACIDIC CATION EXCHANGE RESIONS
- 作者机构：
  
  1. 武汉大学,湖北,武汉,430072
  2. ,湖北,武汉,430072
- 作者简介：
- 基金信息：
- DOI：10.19666/j.rlfd.2003.03.009
  CLC： TM621.8
- Published：2003
- 稿件说明：
移动端阅览
CALCULATION IN WATER TREATMENT DEAIGN FOR JOINTLY USING STRONG AND WEAK ACIDIC CATION EXCHANGE RESIONS[J]. Thermal Power Generation, 2003, (3): 29-32.
DOI：

CALCULATION IN WATER TREATMENT DEAIGN FOR JOINTLY USING STRONG AND WEAK ACIDIC CATION EXCHANGE RESIONS[J]. Thermal Power Generation, 2003, (3): 29-32. DOI： 10.19666/j.rlfd.2003.03.009.

摘要

阐述了强酸与弱酸树脂联合应用的适用条件、设计计算的原则和步骤。其计算方法是按设计流量、周期时间和进水水质、水温等原始条件

以树脂工艺性能曲线和公式为依据

进行若干次试算

最终选出合理的设备类型

并算出设备的直径和强酸与弱酸树脂的层高等。

Abstract

The suitable conditions for jointly using strong and weak acidic cation exchange resins have been expounded. The principle and procedure of calculation in design are given. The calculation is on the basis of operating capacity curves and formulae of the used resins. According to the original conditions

such as designed output

circle time

the temperature and quality of inlet water etc.

trial calculation of several times is needed to select the reasonable equipment

and to calculate the diameter of equipment and the bed heights of strong and weak acidic resins.

关键词

Keywords

references

Views

下载量

CSCD

Alert me when the article has been cited

提交

Publicity Resources

No data

Related Author

No data

Related Institution

No data

AI问答

⁰