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Fine treatment regeneration system and wastewater classified collection method

A regeneration system and fine treatment technology, which is applied in the field of water treatment in thermal power plants, can solve the problems of increasing wastewater volume, mixing, and large water volume, and achieve the effect of increasing the ion concentration of wastewater and reducing the amount of high-salt wastewater

Inactive Publication Date: 2020-04-14
ZHEJIANG ZHENENG TECHN RES INST
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  • Abstract
  • Description
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  • Application Information

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Problems solved by technology

[0004] But the deficiency of current classified collection method is: this kind of classified collection method can make 70% low-salt waste water reuse in regeneration process, but still 30% waste water needs to be treated, and water volume is bigger, and also use desalination process in replacement process. Brine flushing and replacement process still mixed a lot of low-salt wastewater, which not only prevented a large amount of low-salt wastewater from being reused, but also increased the amount of wastewater to be treated in the later stage and increased the cost of post-treatment

Method used

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Embodiment

[0034] Such as figure 2 As shown, in the acid regeneration tank, the process time of the refined cation resin acid regeneration process is 60 minutes, and the desalinated water replacement process time is also 60 minutes. The 0-5 minutes of the regeneration process is mainly to drain the water in the acid resin tank, and the conductivity The rate is 0-200μS / cm; about 5-60 minutes after the regeneration starts, the salt content of the regenerated wastewater increases rapidly, the conductivity rapidly rises from 200-4000μS / cm to 35000-38000μS / cm, and the ammonia nitrogen index changes from 0 to 30 minutes 0mg / L rises to 11000-13000mg / L, and drops to 1000-1200mg / L in 30-60 minutes; 60-80 minutes after regeneration starts, the conductivity drops rapidly from 35000-38000μS / cm to about 800-1000μS / cm, ammonia nitrogen Rapid drop from 1000-1200mg / L to 50-100mg / L; 80-120 minutes after the start of regeneration, the conductivity of the regeneration wastewater dropped from 800-1000μS / cm...

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Abstract

The invention relates to a fine treatment regeneration system and a wastewater classified collection method. The fine treatment regeneration system comprises a resin tank, a wastewater pool, a reuse water pool, an acid regeneration tank, an alkali regeneration tank and valves A, B, C, D, E, F, G and H; the two ends of the resin tank are respectively connected with one end of the valve A and one end of the valve B; the acid regeneration tank is connected with one end of the valve G; the alkali regeneration tank is connected with one end of the valve H; the two ends of the wastewater pool are respectively connected with one end of the valve C and one end of the valve D. The beneficial effects are that: by accurately measuring the change trend of salt content and ammonia nitrogen in fine treatment regeneration process, the part of wastewater with the highest salt content and ammonia nitrogen in the acid / alkali feeding and acid replacement / alkali replacement process is separated out, and the rest part of low-salt wastewater is recycled, so that low-salt wastewater is recycled to the maximum extent. The high-salinity wastewater is separated from the front end, the ion concentration of the wastewater is greatly improved, the high-salinity wastewater amount is reduced by about 40%, and the method has the characteristics of energy conservation and environmental protection.

Description

technical field [0001] The present invention relates to the field of water treatment in thermal power plants, and especially includes a fine treatment regeneration system and a waste water classification and collection method; the precise control of the regeneration process can maximize the reuse of low-salt waste water, and at the same time make the separated high-salt high- The amount of ammonia wastewater is minimized to reduce the burden of subsequent wastewater treatment. Background technique [0002] At present, most of the 300MW or more coal-fired units in service in my country are equipped with condensate polishing systems. At present, the medium-pressure condensate mixed bed system is commonly used, specifically the series connection of the pre-filter and the high-speed mixed bed. The regeneration system mainly includes the separation tower, the negative tower and the positive tower. In addition, it also includes acid and alkali equipment, hot water tank, flushing ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F1/66C02F101/12C02F101/16
CPCC02F1/66C02F2101/12C02F2101/16
Inventor 张贺沈叔云徐浩然陈彪冯向东童小忠高强生王维平余一凡
Owner ZHEJIANG ZHENENG TECHN RES INST
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