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Advanced treatment method for printing and dyeing wastewater

A technology for advanced treatment of printing and dyeing wastewater, applied in water/sewage multi-stage treatment, adsorbed water/sewage treatment, water/sludge/sewage treatment, etc. Achieve the effect of low operating cost, small footprint and no secondary pollution

Inactive Publication Date: 2009-04-08
NANJING UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] The water quality of printing and dyeing wastewater is complex, especially the biochemical-physicochemically treated tail water has poor biodegradability and low concentration of suspended solids. The wastewater mainly contains organic substances that are difficult to degrade biochemically. Traditional physicochemical or biochemical processes have little effect on tail water treatment.
The chemical oxidation method is used for advanced treatment, and the commonly used oxidizing reagents such as chlorine dioxide, hydrogen peroxide oxidation and other chemicals are expensive, resulting in high processing costs; the adsorbents used in the adsorption method include activated carbon, resin, etc., which also have high processing costs and difficult regeneration of the adsorbent. problems; nanofiltration and reverse osmosis, which are commonly used in membrane separation technology, have good treatment effects, and the key technologies and equipment are basically mature, but there are still some problems in the advanced treatment of industrial wastewater, such as expensive membrane materials and short service life , higher power consumption, etc.

Method used

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  • Advanced treatment method for printing and dyeing wastewater

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0020] (1) Preparation of coal filler: the filler is composed of anthracite and pulverized coal with particle size less than 2mm. When preparing the filler, the anthracite is first crushed, and then the pulverized coal with the required particle size is obtained by using a drum sieve with an aperture of 2mm.

[0021] (2) Static adsorption: fill the filler into the adsorption bed, and the ratio of filler to waste water is preferably 1:2.5 to 1:5.

[0022] (3) Process flow: such as figure 1 As shown, the tail water after biochemical treatment of printing and dyeing wastewater is pumped into the static adsorption bed by the water pump after being uniformly adjusted in the water quality and quantity in the adjustment tank, where it is statically adsorbed in the reaction bed for 2 hours, and finally discharged through the outlet pipe at the bottom.

[0023] (4) Process conditions and process parameters: the intermittent operation mode is adopted, and the tail water after biochemic...

Embodiment 2

[0026] (1) Preparation of coal filler: the filler is composed of anthracite and pulverized coal with particle size less than 2mm. When preparing the filler, the anthracite is first crushed, and then the pulverized coal with the required particle size is obtained by using a drum sieve with an aperture of 2 mm.

[0027] (2) Static adsorption: fill the filler into the adsorption bed, and the ratio of filler to waste water is preferably 1:2.5 to 1:5.

[0028] (3) Process flow: such as figure 1 As shown, the tail water after biochemical treatment of printing and dyeing wastewater is pumped into the static adsorption bed by the water pump after being uniformly adjusted in the water quality and quantity in the adjustment tank, where it is statically adsorbed in the reaction bed for 2 hours, and finally discharged through the outlet pipe at the bottom.

[0029] (4) Process conditions and process parameters: the intermittent operation mode is adopted, and the tail water after biochemi...

Embodiment 3

[0032] (1) Preparation of coal filler: the filler is composed of anthracite and pulverized coal with particle size less than 2mm. When preparing the filler, the anthracite is first crushed, and then the pulverized coal with the required particle size is obtained by using a drum sieve with an aperture of 2 mm.

[0033] (2) Static adsorption: fill the filler into the adsorption bed, and the ratio of filler to waste water is preferably 1:2.5 to 1:5.

[0034] (3) Process flow: such as figure 1 As shown, the tail water after biochemical treatment of printing and dyeing wastewater is pumped into the static adsorption bed by the water pump after being uniformly adjusted in the water quality and quantity in the adjustment tank, where it is statically adsorbed in the reaction bed for 2 hours, and finally discharged through the outlet pipe at the bottom.

[0035] (4) Process conditions and process parameters: the intermittent operation mode is adopted, and the tail water after biochemi...

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Abstract

The invention discloses a method which aims at the deep treatment of dyeing wastewater and has the advantages of simple operation, low cost and no secondary pollution. The method comprises the following steps: based on the biochemical-physical and chemical treatment of the dyeing wastewater, tail water obtained after treatment is lifted by a pump and enters a static adsorption bed for filling fine coal particles, the stay time is controlled to between 2 and 4 hours, difficultly degraded organic matters in the tail water are removed by adsorption, and the discharged water meets the discharge standards and is discharged or reutilized. The method has the advantages of unnecessary addition of other chemical agents, low operational cost and no secondary pollution; the stay time is short with no more than 4 hours, and the reactor occupies small areas; the pH value of the tail water does not need to be adjusted, and the tail water after treatment can be reutilized as reclaimed water; and saturated adsorbing materials are unnecessarily regenerated, and can be continuously used as fuel.

Description

technical field [0001] The invention relates to a method for advanced treatment or reuse of printing and dyeing wastewater, which is suitable for advanced treatment or reuse of printing and dyeing tail water after biochemical-physicochemical treatment. Background technique [0002] In 2007, the outbreak of cyanobacteria bloom in Taihu Lake gave birth to the standard of "Discharge Limits of Main Water Pollutants for Urban Sewage Treatment Plants and Key Industries in Taihu Lake Area". The "Taihu New Standard" was officially implemented on January 1, 2008. The scope of implementation includes Wuxi, Changzhou, Suzhou City, Lishui County, Nanjing City, Danyang City, Zhenjiang City, Gaochun County, Jurong City and other Taihu Lake Basins. The third local environmental protection standard issued by the province is stricter than the "national standard". Undoubtedly, the implementation of "Taihu New Standard" will accelerate the restructuring of the textile industry in the Taihu La...

Claims

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Application Information

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IPC IPC(8): C02F9/14C02F1/28
Inventor 夏金雨吴军周正伟曹丽华王娟丁原红
Owner NANJING UNIV
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