Method for treating dye wastewater by utilizing dye intermediate effluent
A dye intermediate and dye wastewater technology, which is applied in chemical instruments and methods, water/sewage multi-stage treatment, water/sludge/sewage treatment, etc., can solve the problems of ineffective utilization and increased dye wastewater treatment cost, etc. To achieve the effect of saving resources, saving costs and reducing environmental pollution
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0023] In the 2000mL beaker, add 1000g COD to be 21280mg / L, chromaticity is the washing waste water of disperse violet 93 dyestuff of 675 times, start stirring, add 80g N-cyanoethylation waste liquid (aluminum chloride content is 10%, for preparation The waste liquid produced in the N-cyanoethylaniline process), stirred at room temperature for 20 minutes, added calcium carbide to adjust the pH value to 10.5, continued to stir for 20 minutes, poured into the vacuum filtration pump for suction filtration, and obtained a light yellow transparent filtrate (pre- treatment liquid), the measured COD is 6250mg / L, the chroma is 153 times, the COD removal rate is 70.63%, and the chroma removal rate is 77.33%.
[0024] like figure 1 As shown, the pretreatment liquid obtained in this embodiment can reach the discharge standard through subsequent oxidation treatment, treatment in the aeration tank and biochemical oxidation treatment.
Embodiment 2
[0026] Add 1000g COD in the 2000mL beaker and be 20630mg / L, chromaticity is the washing waste water of 590 times of disperse orange 288 dyestuffs, start stirring, add 110g N, N-dicyanoethylated waste liquid (aluminum chloride content is 12% , for the waste liquid produced in the process of preparing N,N-dicyanoethylaniline), stirred at room temperature for 20 minutes, added calcium carbide to adjust the pH value to 11.3, continued to stir for 20 minutes, poured into a vacuum filter pump for suction filtration, and obtained Light yellow transparent filtrate, the measured COD is 5590mg / L, the chroma is 125 times, the COD removal rate is 72.90%, and the chroma removal rate is 78.81%. It is directly discharged into the subsequent oxidation tank, aeration tank and biochemical tank for further processing Routine treatment, discharge after reaching the standard.
Embodiment 3
[0028] Adding 1000g COD in the 2000mL beaker is 23600mg / L, chroma is 625 times coupling pot cleaning waste water (color is red), starts stirring, adds 140g N-cyanoethylation waste liquid (aluminum chloride content is 10%, In order to prepare the waste liquid produced in the process of N-ethyl-N-cyanoethylaniline), stir at room temperature for 20 minutes, add calcium carbide to adjust the pH value to 10.8, continue stirring for 20 minutes, and pour it into a vacuum filter pump for suction filtration. Obtain light yellow transparent filtrate, the measured COD is 5630mg / L, the chroma is 116 times, the COD removal rate is 76.14%, the chroma removal rate is 81.44%, and it is directly discharged into the subsequent oxidation tank, aeration tank, biochemical tank Carry out routine treatment and discharge after reaching the standard.
PUM
| Property | Measurement | Unit |
|---|---|---|
| decolorization rate | aaaaa | aaaaa |
Abstract
Description
Claims
Application Information
Login to View More 