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Anolyte clarifying tank waste chlorine gas recovery technology in ionic membrane caustic soda production

A technology of ionic membrane caustic soda and anolyte, applied in the direction of chlorine/hydrogen chloride, chlorine/hydrogen chloride purification, etc., can solve the problems of waste, unrealized utilization of waste acid water, consumption of caustic soda, etc., achieve small investment, normal operation of the production system, avoid The effect of damaging the device

Active Publication Date: 2013-02-13
昊华宇航化工有限责任公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

After the saturated chlorine water enters the anolyte discharge tank, the pressure of the chlorine water changes accordingly, and a large amount of waste chlorine gas escapes. The common practice in the industry is to discharge the waste chlorine gas to the waste chlorine gas absorption tower, and neutralize it with caustic soda for harmless disposal. A large amount of waste sodium hypochlorite solution is produced, and a large amount of caustic soda is also consumed at the same time, so there is a big waste problem
In addition, the daily regeneration of the chelating resin tower in the secondary brine refining process will produce waste acid water, which is directly discharged after neutralization treatment, and the utilization of waste acid water has also not been realized

Method used

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  • Anolyte clarifying tank waste chlorine gas recovery technology in ionic membrane caustic soda production
  • Anolyte clarifying tank waste chlorine gas recovery technology in ionic membrane caustic soda production

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0028] The waste acid water from the regeneration of the resin tower in the secondary brine process first enters the waste water tank, and is slowly sent to the anolyte discharge tank by the waste water pump. The waste acid water enters the waste water tank for 3.5 hours, a total of 30m 3 , control the flow rate of waste acid water to 3.5m 3 / h into the anolyte drain tank. The saturated chlorine water from the chlorine gas scrubber and dechlorination cooler enters the anolyte discharge tank, and reacts with the resin regeneration waste acid water from the waste water tank to decompose a larger amount of chlorine gas. The remote liquid level gauge and frequency conversion controller are all connected to the DCS control system, and the pressure of the chlorine main pipe is -1.3 kPa. The purity of chlorine gas meets the requirements of the production system indicators and can be produced stably.

Embodiment 2

[0030] The waste acid water from the regeneration of the resin tower in the secondary brine process first enters the waste water tank, and is slowly sent to the anolyte discharge tank by the waste water pump. The waste acid water enters the waste water tank for 3.5 hours, a total of 30m 3 , control the flow rate of waste acid water to 4m 3 / h into the anolyte drain tank. The saturated chlorine water from the chlorine gas scrubber and dechlorination cooler enters the anolyte discharge tank, and reacts with the resin regeneration waste acid water from the waste water tank to decompose a larger amount of chlorine gas. The remote liquid level gauge and frequency conversion controller are all connected to the DCS control system, and the pressure of the chlorine main pipe is -1.5 kPa. The purity of chlorine gas meets the requirements of the production system indicators and can be produced stably.

Embodiment 3

[0032] The waste acid water from the regeneration of the resin tower in the secondary brine process first enters the waste water tank, and is slowly sent to the anolyte discharge tank by the waste water pump. The waste acid water enters the waste water tank for 3.5 hours, a total of 30m 3 , control the flow rate of waste acid water to 4.5m 3 / h into the anolyte drain tank. The saturated chlorine water from the chlorine gas scrubber and dechlorination cooler enters the anolyte discharge tank, and reacts with the resin regeneration waste acid water from the waste water tank to decompose a larger amount of chlorine gas. The remote liquid level gauge and frequency conversion controller are all connected to the DCS control system, and the pressure of the chlorine main pipe is -1.2 kPa. The purity of chlorine gas meets the requirements of the production system indicators and can be produced stably.

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Abstract

The invention belongs to the field of waste recycling, and particularly relates to an anolyte clarifying tank waste chlorine gas recovery technology in the ionic membrane caustic soda production. The waste acid water generated by a chelate resin tower of a twice brine purification process is added into an anolyte clarifying tank, and a chlorine gas collection pipeline is added to the original chlorine gas pipeline of the anolyte clarifying tank and joins a chlorine gas manifold to enter the production system. The technology provided by the invention can recycle the waste chlorine gas of the anolyte clarifying tank in the ionic membrane caustic soda production, the chlorine gas purity meets the requirement of greater than or equal to 96% of the production system, and the caustic soda consumption of a waste chlorine gas absorption tower is effectively reduced; and meanwhile, the resin regeneration acid water can be recycled, and the economic and social benefits are relatively great.

Description

technical field [0001] The invention belongs to the field of waste recovery and utilization, and in particular relates to a process for recovering waste chlorine gas from an anolyte cleaning tank in the production of ionic membrane caustic soda. Background technique [0002] At present, the production of caustic soda in China is mainly based on the ionic membrane process. The anolyte discharge tank in the electrolysis process of ionic membrane soda production is one of the continuous operation equipment. . After the saturated chlorine water enters the anolyte discharge tank, the pressure of the chlorine water changes accordingly, and a large amount of waste chlorine gas escapes. The common practice in the industry is to discharge the waste chlorine gas to the waste chlorine gas absorption tower, and neutralize it with caustic soda for harmless disposal. Produce a large amount of waste sodium hypochlorite solution, also consume a large amount of caustic soda simultaneously, ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01B7/07
Inventor 都金贵王银波魏成江慕玉萍潘明明王松波焦高成刘娟张桂香
Owner 昊华宇航化工有限责任公司
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