Method for treating ammonia-nitrogen containing p-aminodiphenyl amine production wastewater

A technology for the production of p-aminodiphenylamine and waste water, which is applied in natural water treatment, water/sewage multi-stage treatment, water/sludge/sewage treatment, etc. It can solve the problem that the COD content does not meet the national discharge standard and lacks complete and effective means , Chlorine leakage in the air and other problems, to achieve stable treatment effect, high ammonia nitrogen removal efficiency, and reduce treatment costs

Active Publication Date: 2014-12-31
CHINA PETROLEUM & CHEM CORP +1
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Problems solved by technology

But this method also has some following problems: first, in the process that chlorine is constantly fed into the inorganic alkali aqueous solution, some chlorine gas will inevitably leak into the air, which will easily cause air pollution; secondly, after being treated by this method, the COD content in the wastewater The national discharge standard has not yet been met; moreover, whether there are other pollutants in the treated wastewater, the patent does not mention
There are some problems in this method: firstly, although the recovery process of formic acid in waste water is described in detail in this patent, whether the treated waste water contains other pollutants is not mentioned in this patent; secondly, the process of recovering formic acid in this method It is very cumbersome, not only need multiple sets of reactors to precipitate calcium formate to prevent the leakage of too much formic acid, but also to add a variety of materials such as Na 2 Additional agents such as S and PAC increase the processing cost
[0006] To sum up, the physical and chemical methods used in the prior art consume a lot of energy for pretreatment of formic acid-containing production wastewater. The chemical oxidation method needs to add chemical oxidants to achieve the purpose of sewage treatment, and the cost of sewage pretreatment is relatively high.
The proposed wastewater reuse point is only in principle, and there is basically no mention of how to deal with the wastewater that needs to be discharged, especially the high-concentration toxic or refractory wastewater.
At present, there is still a lack of methods that can effectively remove organic matter in formic acid-containing wastewater, and there is still a lack of complete and effective means to achieve the standard discharge of ammonia nitrogen-containing p-aminodiphenylamine production wastewater

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  • Method for treating ammonia-nitrogen containing p-aminodiphenyl amine production wastewater

Examples

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Effect test

Embodiment 1

[0070] The wastewater flow rate of a p-aminodiphenylamine production plant in a chemical plant is 100t / d, and the pollutant indicators in the wastewater are: COD of wastewater is 50130mg / L, TOC is 30320mg / L, concentration of formic acid is 116300mg / L, pH is 10.8; wastewater containing ammonia nitrogen The concentration of ammonia nitrogen in the medium is 212mg / L.

[0071] In the first step, in the pH adjustment pool, dilute HCl is used to adjust the pH of p-aminodiphenylamine wastewater to 4.5.

[0072] In the second step, in the homogeneous adjustment tank, p-aminodiphenylamine wastewater (wastewater from the production of p-aminodiphenylamine containing formic acid) is mixed with wastewater containing ammonia nitrogen (wastewater from the production of aniline containing ammonia nitrogen), and the tail magnesium water containing nitrate is added. , and add part of the reflux water from the USB reactor and a small amount of dilution water to dilute the wastewater. The pH of...

Embodiment 2

[0079] The waste water flow rate of a p-aminodiphenylamine production plant in a chemical plant is 110t / d, and the pollutant indicators in the waste water are: waste water COD is 62400mg / L, TOC is 41700mg / L, formic acid concentration is 162600mg / L, pH is 11.4; The concentration of ammonia nitrogen in the wastewater is 276mg / L.

[0080] In the first step, in the pH adjustment pool, dilute HCl is used to adjust the pH of p-aminodiphenylamine wastewater to 4.8.

[0081] In the second step, in the homogeneous adjustment tank, p-aminodiphenylamine wastewater is mixed with wastewater containing ammonia nitrogen, ammonium nitrate wastewater containing nitrate is added, and part of the reflux water from the USB reactor and a small amount of dilution water are added to dilute the wastewater. The pH of the effluent in the homogeneous adjustment tank is 7.1, the COD is 1248.0mg / L, the TOC is 834.0mg / L, the formic acid is 3252.0mg / L, the nitrate is 1273.6mg / L, and the ammonia nitrogen con...

Embodiment 3

[0088] The wastewater flow rate of a p-aminodiphenylamine production plant in a chemical plant is 120t / d, and the pollutant indicators in the wastewater are: wastewater COD is 71500mg / L, TOC is 52620mg / L, formic acid concentration is 228700mg / L, pH is 12.5; The concentration of ammonia nitrogen in the wastewater is 325mg / L.

[0089] In the first step, in the pH adjustment tank, use dilute HNO 3 Adjust the pH of p-aminodiphenylamine wastewater to 5.4.

[0090] In the second step, in the homogeneous adjustment tank, p-aminodiphenylamine wastewater is mixed with ammonia nitrogen-containing wastewater, sodium nitrate solution is added, and part of the reflux water from the USB reactor and a small amount of dilution water are added to dilute the wastewater. The pH of the effluent in the homogeneous adjustment tank is 7.2, the COD is 1430.0mg / L, the TOC is 1052.4mg / L, the formic acid is 4574.0mg / L, the nitrate is 1259.6mg / L, and the ammonia nitrogen concentration is 162.5mg / L. TOC...

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Abstract

The invention relates to a method for treating ammonia-nitrogen containing p-aminodiphenyl amine production wastewater. The method comprises the steps: carrying out pH adjustment on the p-aminodiphenyl amine production wastewater, mixing and homogenizing with phenylamine production wastewater, then adding nitrate-containing wastewater into a homogeneous adjusting tank, completing adjustment of the C / N ratio and the pH value of the mixed wastewater in the homogeneous adjusting tank, next adding N and P nutritive salts into the homogeneous adjusting tank, if effluent of the homogeneous adjusting tank contains more waste residue quantity, requiring to carry out precipitate air flotation treatment on the effluent of the homogeneous adjusting tank, then removing high-concentration organic matters contained in the effluent of the homogeneous adjusting tank through a denitrification reaction, and finally, carrying out a nitration reaction by using the alkalinity generated by the denitrification process to remove ammonia nitrogen in the denitrification reaction effluent. The wastewater treatment method can effectively reduce the organic matters and ammonia nitrogen in the wastewater, substantially cuts down the total amount of pollutants discharged to the environment by a p-aminodiphenyl amine production device, and makes the wastewater reach standards and discharged.

Description

technical field [0001] The invention relates to the treatment of organic chemical wastewater, in particular to a method for treating ammonia nitrogen-containing p-aminodiphenylamine production wastewater. In particular, it refers to a method for denitrifying and nitrifying p-aminodiphenylamine wastewater containing ammonia nitrogen to remove organic matter and ammonia nitrogen, and the p-aminodiphenylamine wastewater contains high-concentration formic acid. Background technique [0002] With the development of economy and society, the demand for rubber additives is increasing. p-Aminodiphenylamine, also known as 4-aminodiphenylamine, N-phenyl-p-phenylenediamine, trade name RT base, as a rubber additive The intermediate is an important dye and rubber auxiliary intermediate, and its main use is to produce p-phenylenediamine antioxidants (for example: rubber antioxidant 4010NA, 4020, 4010, etc.). At present, in the tire manufacturing industry, only two products, 4010NA and 402...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F9/14C02F101/16C02F101/30C02F103/36
Inventor 王珺高凤霞程学文侯秀华张宾莫馗李海龙
Owner CHINA PETROLEUM & CHEM CORP
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