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Method for processing industrial hard biodegradable wastewater based on continuous free-radical generator

A generator and difficult-to-biochemical technology, applied in chemical instruments and methods, water treatment of special compounds, oxidized water/sewage treatment, etc., can solve the problems of not meeting industrial application standards, many bubbles, easy deactivation of catalysts, etc., and achieve Reduce the time of sewage treatment, reduce the BOD/COD value, and reduce the long-term operation cost

Active Publication Date: 2019-10-29
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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  • Method for processing industrial hard biodegradable wastewater based on continuous free-radical generator
  • Method for processing industrial hard biodegradable wastewater based on continuous free-radical generator

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

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

[0043] Mix 100mol melamine and 20mol copper salt to obtain a mixture, then put the mixture into a ball mill for ball milling for 6 hours, pass the ball-milled mixture through a 200-mesh sieve, then vacuum-dry for 3 hours, and finally calcined at 1200°C for 10 hours to obtain Copper-doped carbon nanotubes;

[0044] 2) Dissolve 1mol of molybdic acid and 1mol of ammonium metavanadate in 2L of 0.8mol / L ammonia water to obtain a mixed solution, then add 600g of copper-doped carbon nanotubes prepared in step 1 into the mixed solution, and heat Under ultrasonic treatment for 2 hours, vacuum-dry the slurry after ultrasonic impregnation at 100°C for 10h, the obtained sample is ground and roasted at high temperature in a muffle furnace for a period of time, the roasting temperature is 600°C, and the roasting time is 24h to obtain the powder catalyst MoO3-V2O5 / CNTS.

Embodiment 2

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

[0047] Mix 100mol melamine and 10mol copper salt to obtain a mixture, then put the mixture into a ball mill for ball milling for 6 hours, pass the ball-milled mixture through a 200-mesh sieve, then vacuum-dry for 3 hours, and finally calcined at 1200°C for 10 hours to obtain Copper-doped carbon nanotubes;

[0048] 2) 1mol molybdic acid and 0.5mol ammonium metavanadate are dissolved in 4L concentration and be 0.8mol / L ammonia water to obtain mixed solution, then the copper-doped carbon nanotube prepared in step 1 of 600g is added in the mixed solution, and then in 20 Ultrasonic treatment at ℃ for 2 hours, vacuum-dry the slurry after ultrasonic impregnation at 100℃ for 10h, the obtained sample is ground and roasted at high temperature in a muffle furnace for a period of time, the roasting temperature is 400℃, and the roasting time is 32h to obtain a powder Catalyst MoO3-V2O5 / CNTS.

Embodiment 3

[0061] Treatment of sample sewage:

[0062] The sample sewage is the mixed sewage of tetracycline and oxytetracycline, and the water quality testing index is: CODcr is 10000-28000mg / L, BOD5 / CODcr<0.3.

[0063] according to figure 1 As shown in the device, the granular catalyst prepared in Example 1-2 and Comparative Example 1-2 is packed into the catalyst bed in the fixed-bed reactor 1, and the pressure of the air compressor 3 and the high-pressure buffer tank 2 is adjusted so that it reaches Set the pressure, heat the fixed-bed reactor to the set temperature, and feed air and sample sewage together at a certain feed rate. After 3 hours, carry out COD test and analysis from the reaction solution. The removal rate of COD is shown in Table 1.

[0064] Table 1

[0065]

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Abstract

The invention provides a method for processing industrial hard biodegradable wastewater based on a continuous free-radical generator. Air is adopted as an oxidizing agent, the covering area of equipment is small, the long-term operation cost is low, and the process is safe and controllable; convenience and practicability are achieved, the reaction activity of a catalyst is high, removing of contaminant is thorough, no hazardous gas is generated in the sewage processing process, sludge is not generated, secondary pollution is avoided, COD of inlet water sewage is 8000-100000 mg / L, outlet watercan be directly discharged or enter biochemistry, the removal rate of CODcr can reach up over 95%, and BOD5 / CODcr after processing is larger than 0.3.

Description

technical field [0001] The invention relates to the field of sewage treatment, in particular to a method for treating industrial difficult biochemical sewage based on a continuous free radical generator. Background technique [0002] Since my country began to produce antibiotics in the early 1950s, the output has increased year by year, and it has now become one of the major antibiotic-producing countries in the world. In the production process of antibiotics in my country, there are many deficiencies such as low utilization rate of raw materials, low refining purity, high residual antibiotic content in sewage, etc., resulting in complex components of production sewage, difficult to treat and other problems, causing serious pollution to the environment. [0003] Since antibiotic production sewage is refractory organic sewage, the strong inhibitory effect of residual antibiotics on microorganisms will lead to complex sewage treatment process, high cost and unstable teaching e...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F1/72B01J23/889C02F101/30
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