Treatment process for wastewater in dyeing and finishing industry

A technology for industrial wastewater and treatment process, applied in textile industry wastewater treatment, multi-stage water treatment, water/sewage treatment, etc., can solve the problems of secondary pollution, low investment cost, large dosage, etc., to save construction costs , the effect of saving running time

Inactive Publication Date: 2017-04-26
WUHAN POLYTECHNIC UNIVERSITY
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

(1) Biological method: Biological treatment is widely used in the treatment of urban domestic sewage, but the direct treatment of printing and dyeing wastewater by biological method is greatly affected by the temperature, pH value, dye type, etc. of the wastewater, and it is easy to cause sludge swelling and disintegration of polymer groups etc., resulting in poor treatment effect, and the treated wastewater cannot be discharged up to standard; and printing and dyeing wastewater has high concentration and high toxicity, and direct treatment of wastewater will easily cause the death of bacteria in the sludge, resulting in the failure of wastewater treatment to meet the standard
(2) Physical adsorption method: activated carbon porous adsorption materials are commonly used to adsorb dyes and other substances. It is easily affected by the pH of wastewater, suspended solids in wastewater, polymer pollutants, grease, etc., and the consumption is large and the cost is high; The effect on chromaticity is more obvious, but the ability to remove COD is not strong
o 3 Oxidation method equipment cost is high, dosage is large, Cl 2 The oxidation method is highly toxic and causes secondary pollution; the flocculation method is widely used because of its low investment cost, small equipment footprint, large processing capacity, and high decolorization rate, but some dye wastewater cannot achieve the purpose of decolorization and COD removal by direct flocculation

Method used

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  • Treatment process for wastewater in dyeing and finishing industry

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0011] Wastewater containing a variety of disperse dyes (COD 1500-1800mg / L, pH 5-6) is treated with grids to remove large particles and then enters the adjustment pool 1, and the pH of the wastewater is adjusted to 3-5 with industrial hydrochloric acid Enter the adsorption pool, drop in the broken mushroom cultivation waste in advance in the adsorption pond (the particle size of the broken mushroom cultivation waste is between 0.5-2cm, and it is modified in hydrochloric acid with pH 3-5 for 4 hours in advance), the mushroom cultivation waste and The mass volume ratio of water is 8-10kg / m 3 ;In the adsorption tank, the adsorption time of wastewater and mushroom cultivation waste is 5-6 hours, the temperature is natural, and then settle for 1-2 hours; after adsorption treatment, the removal rate of wastewater color reaches 97%, and the removal rate of COD is 20-35%; The supernatant after sedimentation enters the adjustment tank 2 and mixes with the fabric alkali scouring wastewa...

Embodiment 2

[0013] Wastewater containing a variety of disperse dyes (COD 1500-1800mg / L, pH 5-6) is treated with grids to remove large particles and then enters the adjustment pool 1, and the pH of the wastewater is adjusted to 3-5 with industrial hydrochloric acid Enter the adsorption pool, and put the broken mushroom cultivation waste into the adsorption pond in advance (the mushroom cultivation waste is soaked in hydrochloric acid with a pH of 3-5 to modify it for 4 hours), and the mass volume ratio of the mushroom cultivation waste to water is 10-15kg / m 3 ;In the adsorption tank, the adsorption time of wastewater and mushroom cultivation waste is 5-6 hours, the temperature is natural, and then settle for 1-2 hours; after adsorption treatment, the removal rate of wastewater color reaches 98%, and the removal rate of COD is 30-38%; The supernatant after sedimentation enters the adjustment tank 2 and mixes with the fabric alkali scouring wastewater until the pH is 6-8, then pumps it into t...

Embodiment 3

[0015] Wastewater containing a variety of disperse dyes (COD 1500-1800mg / L, pH 5-6) is treated with grids to remove large particles and then enters the adjustment pool 1, and the pH of the wastewater is adjusted to 3-5 with industrial hydrochloric acid Enter the adsorption pool, and put the broken mushroom cultivation waste into the adsorption pond in advance (the mushroom cultivation waste is soaked in hydrochloric acid with a pH of 3-5 to modify it for 4 hours), and the mass volume ratio of the mushroom cultivation waste to water is 6-10kg / m 3 The adsorption time of wastewater and mushroom cultivation waste in the adsorption pond is 2-3 hours, the temperature is 35°C (the water temperature in the adsorption pond is maintained by the high-temperature wastewater in the workshop), and then settles for 1-2 hours; after the adsorption treatment, the color of the wastewater The removal rate reaches 98.5%, and the COD removal rate is 25-35%. The supernatant after sedimentation enter...

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Abstract

The invention relates to a treatment process for wastewater in a dyeing and finishing industry. The treatment process is characterized by comprising the following steps: a. carrying out grid treatment, namely carrying out the grid treatment on the wastewater containing various types of dispersible dyestuffs to remove large particulate matters; then conveying the wastewater into an adjusting tank 1; b. adjusting the pH (Potential of Hydrogen) value, namely adjusting the pH of the wastewater to be 3-5 with industrial hydrochloric acid and then conveying the wastewater into an adsorption tank; c. adsorbing by mushroom cultivation wastes, namely adding the crushed mushroom cultivation wastes into the adsorption tank in advance and depositing at a natural temperature for 1h-2h, wherein the chroma removal rate of the wastewater subjected to adsorption treatment reaches 97% and the removing rate of COD (Chemical Oxygen Demand) is 20%-35%; and d. treating by an aerobic activated sludge method, namely conveying deposited supernatant into an adjusting tank 2 and mixing the supernatant with textile alkali boiling wastewater until the pH value is 6-8; and pumping the wastewater into an aeration tank, and treating by utilizing the aerobic activated sludge method, wherein the hydraulic retention time is 12 hours.

Description

technical field [0001] The invention relates to a process for treating wastewater in the dyeing and finishing industry. Background technique [0002] The printing and dyeing industry has a large amount of wastewater, high content of organic waste, and deep color. Although the COD is high, the BOD / COD value is small and the biochemical properties are poor. It is recognized as one of the difficult-to-treat industrial wastewater. At present, there are several methods to deal with printing and dyeing wastewater. (1) Biological method: Biological treatment is widely used in the treatment of urban domestic sewage, but the direct treatment of printing and dyeing wastewater by biological method is greatly affected by the temperature, pH value, dye type, etc. of the wastewater, and it is easy to cause sludge swelling and polymer group disintegration etc., which leads to poor treatment effect, and the treated wastewater cannot be discharged up to the standard; and the high concentrat...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F9/14C02F103/30C02F101/16C02F101/30
CPCC02F9/00C02F1/001C02F1/286C02F3/12C02F2101/16C02F2101/308C02F2103/30C02F2301/08
Inventor 梅运军杨明刘骏
Owner WUHAN POLYTECHNIC UNIVERSITY
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