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A device and method for simultaneously removing cod-n-p in an anaerobic biofilm reactor based on iron minerals

A COD-N-P, biofilm reactor technology, used in chemical instruments and methods, anaerobic digestion treatment, biological water/sewage treatment, etc., can solve the problem of limited removal of phosphorus elements, difficult to achieve in engineering, and low phosphorus emission standards and other problems to achieve the effect of preventing sludge loss, reducing scale and reducing loss

Active Publication Date: 2022-02-01
CHINA CONSTR THIRD BUREAU GREEN IND INVESTMENT CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

The premise of this idea is to be able to provide a suitable way of limiting oxygen to achieve a lower oxygen concentration, which usually requires precise control of oxygen aeration, which is difficult to achieve in engineering
At the same time, this idea is also very limited in the removal of phosphorus, and it cannot meet the extremely low phosphorus discharge standards currently stipulated in my country.

Method used

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  • A device and method for simultaneously removing cod-n-p in an anaerobic biofilm reactor based on iron minerals
  • A device and method for simultaneously removing cod-n-p in an anaerobic biofilm reactor based on iron minerals

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Embodiment 1

[0029] Such as figure 1Shown, a kind of anaerobic biofilm reactor based on iron mineral synchronously removes the device of COD-N-P, comprises the biofilm reactor 15 of sealing, is filled with ferric mineral and seeding sewage in the described biofilm reactor 15 The mud 8 is also equipped with a submerged hollow fiber microfiltration membrane module 9, the biofilm reactor is provided with a water inlet, and the submerged hollow fiber microfiltration membrane module is provided with a water outlet, and the water inlet passes through the water inlet pipe 2 and the water inlet The self-priming pump 3 is connected to the sewage tank 1, and the water outlet is connected to the water outlet self-priming pump 14 and the water outlet flowmeter 13. The biofilm reactor is also provided with an automatic electric heating element 4, a monitoring / control element 6, and a dissolved oxygen measuring instrument 7. The monitoring / control element 6 and the dissolved oxygen measuring instrument ...

Embodiment 2

[0031] A method for synchronously removing COD-N-P in an anaerobic biofilm reactor based on iron minerals, in which the sewage in the sewage tank 1 is pumped into the biofilm reactor 15 through the water inlet pipe 2 through the water inlet self-priming pump 3 . Its effective volume is 100cm × 50cm × 20cm, and the total area of ​​the hollow fiber membrane is 0.6 m 2 , filled with 0.8 kg of goethite with a particle size of about 20 microns and 1.2 kg of inoculated sludge, and the flow rate of injected sewage was controlled at 3 kg·COD·M -3 d -1 And the COD concentration in the initial water is 400 mg / L, the ammonia nitrogen concentration is 40 mg / L, and the total phosphorus concentration is 10 mg / L. The automatic electric heating element 4 keeps the water temperature in the sewage treatment area within the range of 34±1°C, the detection / control element 6 and the dissolved oxygen measuring instrument 7 monitor the change of the oxygen content in the sewage treatment area in rea...

Embodiment 3

[0035] A method for synchronously removing COD-N-P in an anaerobic biofilm reactor based on iron minerals, the sewage containing COD concentration of 500 mg / L, ammonia nitrogen concentration of 30 mg / L, and total phosphorus concentration of 8 mg / L was 5kg·COD·M -3 d -1 The flow is transported to the biofilm reactor 15, which is filled with 1 kg of large granular hematite (average particle size is 200 microns) and 1.2 kg of inoculated sludge, keeping the water temperature at 34 ± 1 ℃ range. In the initial stage of sewage injection, the hydraulic retention time is 24 hours, and when the reaction is stable, the hydraulic retention time is 12 hours. The contents of COD, ammonia nitrogen and total phosphorus in the water quality were detected respectively. The measured results showed that the effluent COD concentration was 29.7 mg / L, the ammonia nitrogen concentration was 4.28 mg / L, and the total phosphorus TP concentration was 0.98 mg / L, indicating that the COD removal rate rea...

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Abstract

The invention relates to the technical field of environmental protection and sewage treatment equipment, in particular to a device and method for synchronously removing COD, nitrogen and phosphorus nutrients (COD‑N‑P) in an iron mineral-based anaerobic biofilm reactor, and the device Including a sealed biofilm reactor, the biofilm reactor is filled with ferric minerals and inoculated sludge and equipped with a submerged hollow fiber microfiltration membrane module, the biofilm reactor is provided with a water inlet, and the submerged The hollow fiber microfiltration membrane module is provided with a water outlet. The present invention does not require automatic control equipment to achieve precise oxygen control, and controls the oxidation capacity through the dosage of minerals and the particle size of minerals, so as to realize partial aerobic removal of COD and nitrosation of ammonia nitrogen, and then the denitrifying bacteria will produce Nitrite nitrogen (NO 2 ‑ ‑N) into nitrogen; ferrous ions produced by ferric minerals under the action of iron-reducing bacteria can better remove phosphorus in sewage through precipitation reactions.

Description

technical field [0001] The invention relates to the technical field of environmental protection and sewage treatment equipment, in particular to a device and method for synchronously removing COD-N-P in an anaerobic biofilm reactor based on iron minerals. Background technique [0002] With the rapid development of agriculture and industrialization and the improvement of people's lives, a large amount of domestic sewage, livestock and poultry breeding wastewater and other wastewater containing COD, ammonia nitrogen and phosphorus pollutants have become one of the important factors of water environment pollution. In my country, aerobic secondary biological treatment or biological denitrification and phosphorus removal processes including aerobic aeration are generally used to remove such wastewater, but these conventional biological treatment processes generally have complex processes, large land occupation, high energy consumption, and infrastructure costs. And the problems of...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C02F3/28C02F3/34C02F101/10C02F101/16C02F101/20
CPCC02F3/28C02F3/2866C02F3/34C02F3/346C02F2101/16C02F2101/166C02F2101/203C02F2101/105C02F2209/08C02F2209/14
Inventor 毛旭辉李彦王智成
Owner CHINA CONSTR THIRD BUREAU GREEN IND INVESTMENT CO LTD