COD remover

A technology of remover and adsorbent, which is applied in the field of COD remover, can solve the problems of high treatment cost, complex treatment process, and many investment equipment, and achieve the effect of low comprehensive cost, high treatment efficiency and short coagulation time

Inactive Publication Date: 2019-05-31
黔南高新区绿色化工技术研究院有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Fenton chemical oxidation method is to take hydrogen peroxide as oxidant, a kind of method that organic matter is carried out oxidative degradation under the action of ferrous ion, and its advantage is that operation condition is milder, but its shortcoming is also obvious: 1) because ferrous ion has to hydrogen peroxide Strong catalytic decomposition effect leads to low utilization rate of hydrogen peroxide and high treatment cost; 2) Fenton chemical oxidation method needs to adjust the pH of wastewater to be close to neutral first, so it will consume acid and alkali, and at the same time introduce other types of inorganic salts ; 3) The Fenton chemical oxidation method is mainly to convert refractory organic matter into organic matter that is relatively easy to biochemically degrade. Generally, organic matter cannot be completely degraded, so it can only partially remove COD, and it will enter the biochemical treatment device for secondary degradation. Therefore, this method Usually it can only be used as a pretreatment method for refractory organic wastewater; 4) For high-salt wastewater, after being treated by Fenton chemical oxidation, the content of inorganic salts is not reduced, and it must be diluted to perform biochemical degradation, otherwise bacteria in the biochemical degradation process Unable to adapt to high salt content; 5) High-salt wastewater treated by Fenton chemical oxidation method is not suitable for direct and efficient evaporation desalination, because Fenton method cannot completely degrade organic matter, and these residual organic matter are easy to enter inorganic salts, resulting in desalination after removal Inorganic salts become solid hazardous waste
[0008] Due to the high concentration of this kind of waste liquid, the treatment process is often complicated, the input of equipment is large, and the cost of chemicals is high, which makes the cost of waste liquid treatment too high, which is difficult for ordinary companies to bear. Most companies regard waste liquid with high salt and high COD content as hazardous The high-priced waste is handed over to professional companies for processing, but some companies have taken risks due to cost pressures, illegally and secretly discharged, and directly discharged into the urban pipe network and entered the sewage treatment plant, which seriously affected the normal operation of the urban sewage treatment plant.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0022] A COD remover, the mass parts of each component are: 35 parts of ferrate, 0.1 part of magnesium chloride, 3 parts of aluminum nitrate, 12 parts of polydiallyldimethylammonium chloride, 3 parts of sodium sulfite, 3 parts of sodium nitrate, 1 part of sodium metabisulfite, 12 parts of calcium oxide, 22 parts of activated carbon, the above powder components are uniformly mixed to form a mixture.

[0023] The COD removal method using the above-mentioned composite COD remover is to add the high-salt and high-COD organic wastewater (inorganic salt content 21wt%, COD: 20000mg / L) and the composite COD remover at a ratio of 1:0.003 into the treatment container, Stir evenly at room temperature for 3 minutes and let it stand for 15 minutes, which can make the COD removal rate of high COD wastewater reach 97.6%.

Embodiment 2

[0025] A COD remover, the mass parts of its components are: 55 parts of ferrate, 0.1 parts of magnesium chloride, 12 parts of aluminum sulfate, 11 parts of polydiallyldimethylammonium chloride, 0.1 parts of sodium sulfite, 2 parts of sodium nitrate, 2.5 parts of sodium metabisulfite, 23 parts of calcium oxide, 12 parts of activated carbon, the above powder components are uniformly mixed to form a mixture.

[0026] The COD removal method using the above-mentioned composite COD remover is to add high-salt and high-COD organic wastewater (inorganic salt content 18wt%, COD: 50000mg / L) and the composite COD remover at a ratio of 1:0.008 into the treatment container, Stir uniformly for 3 minutes at room temperature, and let it stand for 15 minutes, which can make the COD removal rate of high COD wastewater reach 98.3%.

Embodiment 3

[0028] A COD remover, the mass parts of its components are: 40 parts of ferrate, 0.2 parts of magnesium chloride, 1 part of ferric chloride, 3 parts of polydiallyldimethylammonium chloride, 6.5 parts of sodium sulfite, 2 parts of sodium nitrite, 1.5 parts of sodium metabisulfite, 25 parts of calcium oxide, 105 parts of molecular sieve, the above powder components are uniformly mixed into a mixture.

[0029] The COD removal method using the above composite COD remover is to add the high-salt and high-COD organic wastewater (inorganic salt content 10wt%, COD: 50000mg / L) and the composite COD remover at a ratio of 1:0.005 into the treatment container, Stir evenly at room temperature for 3 minutes and let it stand for 15 minutes, which can make the COD removal rate of high-COD wastewater reach 97.5%.

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Abstract

The invention discloses a COD remover. Ferrate is taken as a main agent and is compounded with an organic flocculant and a metal salt as auxiliary materials, the coagulation time is short, the COD remover is suitable for high-salt high-COD organic wastewater treatment of various processes, the treatment efficiency is high, the comprehensive cost is low, and the removal rate of COD is 97% or above.

Description

Technical field [0001] The invention belongs to the technical field of organic wastewater treatment, and specifically relates to a COD remover. Background technique [0002] Since the 1990s, with the rapid development of my country's textile industry, the printing and dyeing industry has expanded rapidly, and the production and use of dyes have increased. As a result, a large amount of dye wastewater with high COD, high chroma, high toxicity, high salinity, and low B / C is produced. According to statistics, the total amount of dye wastewater produced by the printing and dyeing industry in 2009 has reached 2.43 billion tons, accounting for more than 80 shares of the total discharge of wastewater from the textile industry. This kind of dye wastewater has the characteristics of "four highs and one low" and is related to the types of dyes used. At the same time, in the production of dyes, the enrichment of salts in the discharged wastewater is mainly caused by the production process...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F1/56C02F1/52C02F1/28C02F103/30C02F101/30C02F103/34
Inventor 周春松胡成坤贾建洪王荔郭金栋孙坚
Owner 黔南高新区绿色化工技术研究院有限公司
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