Advanced treatment process for paper-making waste water

A papermaking wastewater and advanced treatment technology, applied in the field of decolorization process, can solve the problems of insufficient decolorization, high power consumption, and high cost, and achieve the effects of saving operating costs, good conductivity, and low cost

A papermaking wastewater and advanced treatment technology, applied in the field of decolorization process, can solve the problems of insufficient decolorization, high power consumption, and high cost, and achieve the effects of saving operating costs, good conductivity, and low cost

CN101337752AActive Publication Date: 2009-01-07HUATIAN ENG & TECH CORP MCC

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  • Advanced treatment process for paper-making waste water

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Embodiment Construction

[0021] A papermaking wastewater advanced treatment process, the process comprises the following steps:

[0022] ①Introduce the papermaking wastewater after the secondary biochemical treatment into the micro-aeration iron reduction bed, fill the iron filings in the micro-aeration iron reduction bed, and carry out the reduction reaction in the micro-aeration iron reduction bed for the papermaking wastewater;

[0023] ②Introduce the effluent treated in step ① into the coagulation tank, and add coagulant and coagulant aid in the coagulation tank to promote the aggregation of particles in the water;

[0024] ③Introduce the effluent treated in step ② into the sedimentation tank for mud-water separation;

[0025] ④The effluent from the sedimentation tank is introduced into the filter tank for filtration, and the filtered effluent is sterilized and then introduced into the reuse water pipe network;

[0026] ⑤The sludge in the sedimentation tank and the backwash sewage in the filter t...

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Abstract

The invention discloses an advanced treatment process of paper-making wastewater. The process comprises the following steps: introducing the paper-making wastewater after being subjected to secondary biochemical treatment into a micro-aeration iron reduction bed, backfilling iron chips in the micro-aeration iron reduction bed, and carrying out reducing reaction to the paper-making wastewater in the micro-aeration iron reduction bed; introducing effluent water after being processed according to step one into a coagulation basin, and adding a coagulating agent and a coagulant aid to the coagulation basin, so as to promote grains in the water to be agglomerated; introducing effluent water after being processed according to step two to a sedimentation tank for sludge separation; introducing the effluent water in the sedimentation tank into a filter basin for being filtered; introducing the effluent water filtered after being sterilized and disinfected into a reusing water pipe network; introducing sludge in the sedimentation tank and back washing blow-off water in the filter basin into a sewage thicker, and outwardly transporting the sludge and the back washing blow-off water after being dehydrated for disposal; and meanwhile, introducing dehydrate filtrate solution and overflowing liquid in the sewage thicker into the coagulation basin for re-treatment. The process has the advantages of simple process, good decoloration effect and cheap cost.

Description

technical field [0001] The invention relates to a method for recycling papermaking wastewater after advanced treatment, in particular to a decolorization process for advanced treatment of papermaking wastewater after secondary biochemical treatment. Background technique [0002] Papermaking industrial wastewater is a difficult industrial wastewater with high chroma, high alkalinity, high organic pollutants, and low biodegradability. The wastewater contains a variety of hydrocarbons, phenols, acids, benzene, anthracene, quinones and other organic substances and their derivatives , polymers, halogenated substances, especially lignin are difficult to biodegrade. Papermaking enterprises generally carry out secondary biochemical treatment or even tertiary treatment of their wastewater, but the chemical oxygen demand (COD for short) of the effluent is generally above 150mg / L, and the dilution factor of the chroma is greater than 64 times. Biochemical Oxygen Demand (BOD) 5 ) is u...

Claims

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Application Information

Patent Timeline
07 Jan 2009
Publication
CN101337752A
IPC
C02F9/14; C02F1/70; C02F1/52; C02F1/50; C02F11/12; C02F103/28
Inventors
陈祥宏; 程寒飞