A zero discharge water treatment system continuous ion exchange softening process

By optimizing the continuous ion exchange unit and countercurrent regeneration technology, the problems of continuous operation and resource utilization of the ion exchange hardening method in the zero-emission system have been solved, reducing equipment investment and operating energy consumption, and achieving stable water treatment effect and resource recovery.

CN122403555APending Publication Date: 2026-07-17CHINA COAL TECH & ENG GRP HANGZHOU ENVIRONMENTAL PROTECTION INST
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Patent Information

Application Number
CN202610624276.X
Authority / Receiving Office
CN · China
Patent Type
Applications(China)
Current Assignee / Owner
Filing Date
2026-05-08
Publication Date
2026-07-17

AI Technical Summary

Technical Problem

Existing ion exchange hardening methods in zero-emission systems suffer from problems such as insufficient continuous operation capability, high regeneration cost, significant safety risks, and resource waste. In particular, in coal chemical and mine water treatment, traditional ion exchange hardening technology operates intermittently, has high regenerant costs and significant pollution risks, and low resource utilization efficiency.

Method used

By optimizing the structure of a continuous ion exchange device and using sodium sulfate concentrate generated by a membrane concentration system as a regenerator, countercurrent regeneration is achieved. The regeneration process is optimized through an adsorption-two-stage synergistic regeneration-cleaning method, reducing equipment investment and operating energy consumption, and improving resource utilization.

Benefits of technology

It enables the simultaneous operation of continuous hardening treatment and resin regeneration, reduces equipment investment and operating energy consumption, improves resource utilization, ensures the stable operation of the membrane concentration system, and reduces solid waste treatment costs.

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Abstract

本发明公开了一种零排放水处理系统连续离子交换除硬方法,步骤包括:原水及再生树脂进入吸附柱进行吸附处理;吸附处理后的树脂进入一级再生柱进行初级再生,再生液为硫酸钠溶液;初级再生后的树脂进入二级再生柱进行深度再生,再生液为硫酸钠溶液;深度再生后的树脂进入清洗柱用清水冲洗得到再生树脂,返回吸附柱使用;一级再生柱和二级再生柱内设有中心筒,再生液和树脂形成逆流接触。本发明通过优化连续离子交换装置结构实现逆流再生,配合膜浓缩系统产生的硫酸钠浓缩液作为再生剂,实现连续除硬处理与离子交换树脂的连续再生,可最大化再生效率,同时显著降低设备投资成本。
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Citation Information

Patent Citations

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