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A method for treating industrial difficult-to-biochemical sewage based on a continuous free radical generator

A generator, biochemically difficult technology, applied in chemical instruments and methods, oxidized water/sewage treatment, special compound water treatment, etc. Achieve low long-term operating costs, process safety and controllability, and small footprint

Active Publication Date: 2021-07-27
宜兴国际环保城科技发展有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the disadvantages of the ordinary activated sludge method are: the sewage needs to be diluted in large quantities, there are many air bubbles during operation, sludge expansion is easy to occur, the amount of residual sludge is large, and the removal rate is not high, so secondary or multi-stage treatment must be often used
Patent CN108579753A discloses an antibiotic sewage pipe type free radical oxidation catalyst, but the catalyst activity is low, the COD removal rate cannot meet the industrial requirements and the catalyst is easy to deactivate, which is far from the industrial application standard

Method used

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  • A method for treating industrial difficult-to-biochemical sewage based on a continuous free radical generator
  • A method for treating industrial difficult-to-biochemical sewage based on a continuous free radical generator

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0042] 1) Preparation of copper-doped carbon nanotubes:

[0043] 100 mol of melamine and 20 mol of copper salts were mixed to obtain a mixture, and then the mixture was placed in a ball mill for 6 hours, and the mixture after the ball was over 200 mesh sieve, and then dried in vacuo for 3 hours, and finally calcined at 1200 ° C for 10 hours. Copper-doped carbon nanotubes;

[0044] 2) 1 mol of molybdate and 1 mol vanadanate is dissolved in a mixed solution in a 2 L concentration of 0.8 mol / L ammonia, and then the copper-doped carbon nanotubes prepared by 600 g of step 1 were added to the mixed solution, and then 20 ° C The lower ultrasound treatment is 2 hours, and the slurry after ultrasonic impregnation is dried in 15 hours, and the obtained sample is calcined in a high temperature of the muffle in the muffle furnace for a period of time, the calcination temperature is 600 ° C, the calcination time is 24 h, which is powdered catalyst MOO3-V2O5 / CNTs.

Embodiment 2

[0046] 1) Preparation of copper-doped carbon nanotubes:

[0047] 100 mol of melamine and 10 mol copper salts were mixed, and then the mixture was placed in a ball mill for 6 hours, and the mixture after the ball was over 200 mesh sieve, and then dried in vacuo for 3 hours, and finally calcined at 1200 ° C for 10 hours. Copper-doped carbon nanotubes;

[0048] 2) 1 mol of molybdate and 0.5 mol vanadate is dissolved in a 4L concentration of 0.8 mol / L ammonia to obtain a mixed solution, and then the copper-doped carbon nanotubes prepared by 600 g of step 1 were added to the mixed solution, and then 20 Ultrasonic treatment at ° C for 2 hours, the slurry after ultrasonic impregnation was dried in vacuo at 100 ° C for 10 h, and the resulting sample was calcined at a high temperature in the muffle furnace for a period of time, the calcination temperature was 400 ° C, the calcination time was 32 h, which is powdered Catalyst MoO3-V2O5 / CNTs.

Embodiment 3

[0061] Sample sewage treatment:

[0062] Sample sewage is a mixed sewage of tetracycline and oxytes, and water quality test indicators is: CODCR is 10,000 ~ 28000mg / L, BOD5 / CODCR <0.3.

[0063] according to figure 1 The apparatus shown, the particulate catalyst prepared in Examples 1-2 and the Comparative Example 1-2 is loaded into the catalyst bed in the fixed bed reactor 1, and the pressure of the air compressor 3 and the high pressure buffer can 2 is adjusted to achieve it. Set the pressure, heat the fixed bed reactor to rise to the set temperature, air and sample sewage feed together with a certain feed velocity, from the reaction liquid, COD test analysis, COD removal rate is shown in Table 1.

[0064] Table 1

[0065]

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Abstract

The invention provides a method for treating industrial difficult-to-biochemical sewage based on a continuous free radical generator. Air is used as an oxidant, the equipment occupies a small area, the long-term operation cost is low, and the process is safe and controllable; The removal of pollutants is thorough, no toxic and harmful gases are produced during the sewage treatment process, no sludge is produced, and there is no secondary pollution. The influent sewage COD is 8000-100000mg / L, and the effluent can be directly discharged or enter the biochemical process. The CODcr removal rate can reach up to 95 % or more, BOD5 / CODcr>0.3 after treatment.

Description

Technical field [0001] The present invention relates to the field of sewage treatment, and more particularly to a method of treating industrial difficulty sewage based on a continuous radical generator. Background technique [0002] Since the production of antibiotics since the 1950s, my country has increased annual birth year, and now it has become one of the main antibiotic drug producing countries in the world. In the production process, my country's antibiotics has a low raw material utilization rate, low purity, and has a higher incidence of residual antibiotics in sewage, thereby causing complicated production of sewage ingredients, difficult to treat, and cause severe pollution to the environment. [0003] Since antibiotic production sewage belongs to difficult degradation organic sewage, the strong inhibitory effect of residual antibiotics on microorganisms can result in complex, high cost, high cost and teaching effect. Therefore, in the treatment of antibiotic sewage, p...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/00C02F101/30
CPCB01J23/8892C02F1/72C02F2101/30C02F2305/023
Inventor 周春松贾建洪孙坚
Owner 宜兴国际环保城科技发展有限公司