Membrane bioreactor and wastewater treatment method for simultaneous anammox and methane production

A membrane bioreactor, anaerobic methane production technology, applied in chemical instruments and methods, sustainable biological treatment, aerobic and anaerobic process treatment, etc., can solve the problems of unable to remove ammonium nitrogen, reduce, affect biological activity, etc.

Active Publication Date: 2022-07-12
广东嘉园生物技术有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

This biological treatment process is often difficult to work. The reason is that the high concentration of ammonium nitrogen in the pig farm sewage affects the biological activity of the aerobic activated sludge process. In the anaerobic digester, a large amount of organic matter is converted by anaerobic bacteria into Methane and carbon dioxide, the concentration of organic matter in the anaerobic effluent is significantly reduced, and the series of metabolic reactions of anaerobic digestion cannot remove ammonium nitrogen in the water body. On the contrary, the hydrolysis reaction decomposes the influent suspended matter into ammonium and dissolved organic matter, so that the anaerobic digestion tank The ammonium concentration in the effluent does not fall but rises

Method used

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  • Membrane bioreactor and wastewater treatment method for simultaneous anammox and methane production

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Embodiment 1

[0040] The microbial carrier is formed by mixing polysulfone particles and polyethylene glycol gel particles in a 3:2 manner, the pore size of the microbial carrier is 4-5 μm, and the porosity is 92%, and the dosage of the microbial carrier accounts for 1 / 5 of the volume of the anaerobic methanogenesis reactor 3.

[0041] The method for wastewater treatment using the synchronous anammox and methane-producing membrane bioreactors comprises the following steps:

[0042] Step S1: transport the sewage into the water inlet pool 1, and dilute to an organic concentration of 2200 mg(COD) / L~2500 mg(COD) / L;

[0043] Step S2: add the microbial carrier into the anaerobic methanogenesis reactor 3, start the water inlet pump 2, and transport the sewage in the water inlet pond 1 to the water distribution pipe 4 at the bottom of the anaerobic methanogenesis reactor 3, and spray from the water distribution hole. The discharged sewage forms an upward flow, which is fully contacted with the mic...

Embodiment 2

[0051] The microbial carrier is formed by mixing cellulose acetate particles, polyvinyl alcohol gel particles and polyurethane particles in a 2:2:1 manner. The pore size of the microbial carrier is 3-4 μm and the porosity is 90%. The dosing amount accounts for 1 / 4 of the volume of the anaerobic methanogenesis reactor 3 .

[0052] The method for wastewater treatment using the synchronous anammox and methane-producing membrane bioreactors comprises the following steps:

[0053] Step S1: the sewage is transported into the water inlet pool 1, and diluted to an organic concentration of 2400mg(COD) / L~2800mg(COD) / L;

[0054] Step S2: add the microbial carrier into the anaerobic methanogenesis reactor 3, start the water inlet pump 2, and transport the sewage in the water inlet pond 1 to the water distribution pipe 4 at the bottom of the anaerobic methanogenesis reactor 3, and spray from the water distribution hole. The discharged sewage forms an upward flow, which is fully contacted ...

Embodiment 3

[0062] The microbial carrier adopts polyvinylidene chloride particles, the pore size of the microbial carrier is 6-8 μm, the porosity is 88%, and the dosage of the microbial carrier accounts for 1 / 3 of the volume of the anaerobic methanogenesis reactor 3 .

[0063] The method for wastewater treatment using the synchronous anammox and methane-producing membrane bioreactors comprises the following steps:

[0064] Step S1: the sewage is transported into the water inlet pool 1, and diluted to an organic concentration of 2100mg(COD) / L~2400mg(COD) / L;

[0065] Step S2: add the microbial carrier into the anaerobic methanogenesis reactor 3, start the water inlet pump 2, and transport the sewage in the water inlet pond 1 to the water distribution pipe 4 at the bottom of the anaerobic methanogenesis reactor 3, and spray from the water distribution hole. The discharged sewage forms an upward flow, which is fully contacted with the microbial carrier until the sewage fills the anaerobic met...

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Abstract

The invention discloses a membrane bioreactor for simultaneous anaerobic ammonia oxidation and methane production and a wastewater treatment method. The sewage is diluted and then transported to an anaerobic methane production reactor. A microbial carrier with a porosity of 10 μm and a porosity of more than 80%. The anammox bacteria on the microbial carrier are used to convert nitrite nitrogen and ammonia nitrogen in sewage into nitrogen and nitrate nitrogen after domestication, and the first return path is connected. The activated sludge aerobic zone and the activated sludge anoxic zone, the second return path connects the activated sludge anaerobic zone and the activated sludge anoxic zone, and the third return path connects the activated sludge anoxic zone and the activated sludge aerobic zone zone, the sludge mixture in the activated sludge anoxic zone can be returned to the anaerobic methanogenesis reactor, activated sludge anaerobic zone, activated sludge through the first return path, the second return path and the third return path The return port of the anoxic zone enables sewage and activated sludge to undergo three processes of hydrolysis, acidification, acid production and methane production under anaerobic conditions.

Description

technical field [0001] The invention relates to the field of sewage treatment systems, in particular to a membrane bioreactor for simultaneous anaerobic ammonium oxidation and methane production and a wastewater treatment method. Background technique [0002] Pig farm sewage contains high concentrations of organic matter, with a chemical oxygen demand of up to 8000mg(COD) / L, as well as a large amount of nutrients such as nitrogen and phosphorus. The total nitrogen content can be as high as 1900mg(N) / L and the total phosphorus content can be as high as 150mg ( P) / L. Once the sewage from pig farms enters the surface water, it will cause severe hypoxia in the surface water, the death of aquatic organisms, and also cause eutrophication of the water, resulting in soil and groundwater pollution and other environmental impacts. [0003] At present, the treatment of pig farm sewage mainly includes biological treatment methods such as anaerobic digestion and aerobic activated sludge...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C02F3/30C02F101/30
CPCC02F3/30C02F2101/30Y02W10/10
Inventor 曾一鸣
Owner 广东嘉园生物技术有限公司
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