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A method for returning aerobic effluent to an anaerobic reactor for dilution and anaerobic ammonium oxidation for treating gas wastewater

An anaerobic reactor and anaerobic ammonium oxidation technology, which is applied in the field of anaerobic ammonium oxidation treatment of gas wastewater, can solve the problems of not being able to become the genus of opulent bacteria, nitrosating bacteria can not get the advantage, and the nitrosation reaction cannot be carried out. To achieve the effect of improving inhibition and improving biodegradability

Inactive Publication Date: 2016-04-27
NORTHEAST DIANLI UNIVERSITY
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  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

The feature of this process is to stably control the nitrification process in the nitrosation stage, with NO 2 — —N is the end product of nitrification, compared with the traditional nitrification-denitrification process, it can save 25% of oxygen supply and 40% of methanol (external carbon source), but in the SHARON process, it is also necessary to carry out the nitrification reactor At the same time, the nitrosating bacteria are autotrophic bacteria. When the concentration of organic matter in the nitrification reactor water is too high, the heterotrophic bacteria with a high proliferation rate will proliferate rapidly, so that the autotrophic nitrosating bacteria can be obtained. If there is no advantage, it cannot become a dominant genus, and the nitrosation reaction will eventually fail to proceed

Method used

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  • A method for returning aerobic effluent to an anaerobic reactor for dilution and anaerobic ammonium oxidation for treating gas wastewater
  • A method for returning aerobic effluent to an anaerobic reactor for dilution and anaerobic ammonium oxidation for treating gas wastewater
  • A method for returning aerobic effluent to an anaerobic reactor for dilution and anaerobic ammonium oxidation for treating gas wastewater

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Embodiment 1

[0026]Embodiment 1: refer to figure 1 , the present invention is a kind of method that aerobic effluent returns to anaerobic reactor to dilute and treat gas waste water by anaerobic ammonium oxidation, the waste water that total water quantity is Q is divided into two parts, the waste water of fQ enters hydrolysis acidification reactor, and another part (1-fQ) The raw wastewater and part of the effluent RQ of the aerobic reactor enter the anaerobic reactor, and the effluents of the anaerobic reactor and the hydrolysis acidification reactor enter the aerobic reactor together, and then the effluent of the aerobic reactor into the anoxic reactor. The hydrolytic acidification reactor can achieve the purpose of improving the biodegradability of raw wastewater; the anaerobic reactor can not only remove organic matter, but also dilute the anaerobic influent concentration and reduce the concentration of raw wastewater through the reflux of the effluent from the aerobic reactor. Toxi...

Embodiment 2

[0027] Embodiment 2, with reference to figure 2 , Embodiment 2 is substantially the same as Embodiment 1. The difference from Example 1 is that the anaerobic reactor is equipped with two stages, (1-fQ) raw wastewater and part of the effluent RQ of the aerobic reactor enter the first-stage anaerobic reactor A1, and the effluent of the anaerobic reactor A1 enters In the secondary anaerobic reactor A2, the reason for this setting is that the primary anaerobic reactor A1 mainly removes easily biodegradable organic matter, while achieving the effect of the anaerobic reactor in Example 1. The setting of the secondary anaerobic reactor A2 is mainly to further degrade the refractory organic matter that was not removed in the primary anaerobic reactor A1, so the purpose of setting the two-stage anaerobic reactor is to achieve the maximum degradation of organic matter and reduce the The toxicity of wastewater improves a stable environment for the operation of the aerobic section, and ...

Embodiment 3

[0028] Embodiment 3: refer to image 3 , Embodiment 3 is substantially the same as Embodiment 2. The difference is that the effluent part of the aerobic reactor is returned to the anaerobic reactor A2, which can dilute the concentration and toxicity of the refractory organic matter in the primary anaerobic reactor A1 and enter the secondary anaerobic reactor A2, which is beneficial The metabolic work activity of anaerobic bacteria in the secondary anaerobic reactor A2 is increased, and at the same time, the purpose of anaerobic ammonium oxidation is realized, so that the function of the secondary anaerobic reactor A2 can be fully exerted.

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Abstract

The invention relates to a gas wastewater treatment method characterized by returning aerobiotic effluent to an anaerobic reactor to be diluted and subjected to anaerobic ammonia oxidation. In the method, an anaerobic reactor, a hydrolytic acidification reactor, an aerobiotic reactor, an oxygen-deficiency reactor are used. Water the quantity of which is fQ enters the hydrolytic acidification reactor directly, wherein Qf means that the total quantity (Q) of raw wastewater is multiplied by a distribution factor (f); the rest raw wastewater the quantity of which is (1-fQ) and water which returns from the aerobiotic reactor and the quantity of which is RQ enter the anaerobic reactor; ammonia nitrogen entering the hydrolytic acidification reactor is divided; after entering the aerobiotic reactor, the wastewater can generate nitrate nitrogen and nitrite nitrogen under the action of aerobiotic nitrifying bacteria; and effluent from the aerobiotic reactor returns to the anaerobic reactor and is reduced into nitrogen gas by using ammonia nitrogen under the action of anaerobic ammonium oxidation bacteria. The method is characterized in that the effluent from the aerobiotic reactor returns to the anaerobic reactor at a reflux ratio R of 0-100%. The method is scientific and reasonable, is simple in flow, low in operation cost, capable of fully degrading organics in the wastewater, good in water treatment effect and can be popularized and applied conveniently.

Description

technical field [0001] The invention relates to the technical field of sewage and wastewater treatment, and relates to a method for returning aerobic effluent to an anaerobic reactor for dilution and anaerobic ammonium oxidation treatment of gas wastewater. Background technique [0002] The new coal chemical technology is a clean utilization technology of coal. It takes coal gasification as the leader and carbonization technology as the basis to synthesize and produce various chemical products and fuel oil. The wastewater discharged mainly comes from processes such as coal coking, gas purification and chemical product recovery and refining. Coal chemical wastewater has complex components, high ammonia and high phenol, high chroma and toxicity, and poor biodegradability. At the same time, coal chemical wastewater also contains a lot of organic matter with chromophores and auxochromes, which makes coal chemical wastewater have the characteristics of high chroma and turbidity....

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C02F9/14
CPCC02F3/02C02F3/08C02F3/28C02F3/2826C02F3/2833C02F3/284C02F3/2846C02F3/302C02F9/00
Inventor 杨世东廖路花王伟卓张兰河崔凤国
Owner NORTHEAST DIANLI UNIVERSITY
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