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A combined process and treatment system for high ammonia nitrogen wastewater treatment

A wastewater treatment and combined process technology, which is applied in the field of combined processes and treatment systems for high-ammonia nitrogen wastewater treatment, can solve the problems of increasing biological disc plates, complex process flow, limiting the effect of pollutant treatment, etc. The effect of adsorption, strengthening denitrification and phosphorus removal efficiency, and improving process treatment effect

Active Publication Date: 2022-07-12
CHONGQING UNIV OF TECH
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  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0012] 1. The advanced treatment process with a large processing capacity has certain requirements on the diameter of the biological disk. The larger the wastewater treatment volume, the larger the diameter of the disk, or the more turntable groups are required, which will not only increase the occupation Land area, adding more bio-disc plates, increasing infrastructure costs;
[0013] 2. If the low-temperature high-ammonia-nitrogen wastewater below 15-18°C is to be treated, the biological turntable system needs to be built indoors or buried underground, and a heating device is added at the same time, which increases the operating cost and infrastructure cost
[0014] 3. After the livestock and poultry breeding wastewater is treated by anaerobic fermentation, although most of the COD (organic matter) is removed, the ammonia nitrogen only changes in form, and the concentration is still high, forming low-carbon and high-ammonia nitrogen wastewater (biogas slurry), biological turntable wastewater treatment When the system treats low-carbon high-ammonia-nitrogen wastewater (biogas slurry), the microbial resistance to high ammonia-nitrogen is poor. Due to the serious imbalance of the C / N ratio in the biogas slurry, the insufficient carbon source will lead to poor denitrification effect of the biological turntable wastewater treatment system. If you want to continue to carry out advanced processing, it will inevitably complicate the subsequent process and increase the processing cost
These methods improve the biodegradability and denitrification effect of the biogas slurry to a certain extent, often at the cost of increasing the energy consumption and cost per unit of wastewater treatment. For large-scale farms with an average daily wastewater production of hundreds of tons, the operating cost is too high. High, unable to afford, resulting in the long-term problem of wastewater treatment in livestock and poultry farms that is difficult to effectively solve
[0017] The biological contact oxidation advanced treatment unit has the characteristics of strong impact load resistance and no need for reflux, and the contact oxidation filler has a large specific surface area and adsorption performance, and has a good oxygen mass transfer coefficient. It is widely used in the treatment of low-carbon high Ammonia nitrogen organic wastewater (biogas slurry), but high ammonia nitrogen has a strong toxic effect on microorganisms, and most organic wastewater has poor biodegradability, resulting in unsatisfactory denitrification and organic matter removal effects. Nitrogen and phosphorus removal function, which limits the effect of pollutant treatment

Method used

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  • A combined process and treatment system for high ammonia nitrogen wastewater treatment
  • A combined process and treatment system for high ammonia nitrogen wastewater treatment
  • A combined process and treatment system for high ammonia nitrogen wastewater treatment

Examples

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Effect test

Embodiment 1

[0061] According to the above steps, the raw water of a pig farm in Banan, Chongqing is subjected to solid-liquid separation of manure residue and waste liquid through a centrifugal separator, and the supernatant is taken as influent water, which is sequentially passed through the biological turntable pretreatment unit 300 to contact with the biological The oxidation advanced treatment unit 400 has a treatment capacity of 100L / d.

[0062] During the operation of the treatment system, keep the ambient temperature at 25-28°C, set the hydraulic retention time of the biological turntable pretreatment unit 300 to 24h, and use four turntables 301 for grading treatment. The water end 305 to the water outlet end 306 are arranged in order. The rotational speed of the first turntable at the water inlet end is 100rpm / min, the rotational speed of the second turntable is 60rpm / min, the rotational speed of the third turntable is 30rpm / min, and the rotational speed of the turntable at the wat...

Embodiment 2

[0068] After the pig farm wastewater is treated by anaerobic fermentation, the biogas slurry produced has the characteristics of high ammonia nitrogen and low carbon nitrogen ratio. The two major treatment difficulties of traditional denitrification technology are: high ammonia nitrogen is biologically toxic and inhibits the growth of microorganisms; biogas slurry has low organic matter concentration and poor biodegradability, resulting in C / N imbalance, which cannot provide sufficient carbon source for microorganisms, making wastewater denitrification. Nitrogen is ineffective.

[0069] The combined process of the invention is used to treat the biogas slurry of a high-breed pig farm in Banan, Chongqing. After the biogas slurry is processed by the biological turntable pretreatment unit and the biological contact oxidation advanced treatment unit in turn, the effluent of the coagulation and sedimentation unit can meet the discharge standard. The specific processing situation is ...

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Abstract

The invention discloses a combined process for the treatment of high ammonia nitrogen wastewater, which comprises the following steps: solid-liquid separation → biological turntable pretreatment → biological contact oxidation advanced treatment → coagulation and sedimentation. The biological turntable pretreatment unit of the treatment system adopted in the process is adopted A plurality of turntables are supported on the same rotating shaft. Each turntable is driven by a planetary gear reducer with different transmission ratios. The rotation speed of the turntable is gradually reduced from the water inlet to the water outlet. The gas device adjusts the dissolved oxygen concentration of the high ammonia nitrogen waste liquid, so that the pretreatment system has a higher pollutant load, and the biological contact oxidation advanced treatment unit is equipped with several contact oxidation fillers, which rely on the iron-carbon micro-electrolysis-activated carbon fiber combination. The characteristics of electrolysis and biofilm degradation enhance the efficiency of nitrogen and phosphorus removal in the system, especially when dealing with low-carbon and high-ammonia-nitrogen wastewater (biogas slurry), overcoming the serious imbalance of the C / N ratio in the biogas slurry and improving the treatment efficiency of high-ammonia-nitrogen wastewater .

Description

technical field [0001] The invention relates to the technical field of wastewater treatment, in particular to a combined process and a treatment system for treating high-ammonia-nitrogen wastewater. Background technique [0002] Rural non-point source pollution refers to dissolved or solid pollutants in rural life and agricultural production activities, such as soil particles, nitrogen, phosphorus, pesticides, heavy metals, and rural livestock manure in farmland. With organic or inorganic substances such as household garbage, from non-specific areas, under the action of precipitation and runoff erosion, through farmland surface runoff, farmland drainage and underground leakage, a large number of pollutants enter the receiving water bodies (rivers, lakes, reservoirs, pollution caused by the bay). At present, the organic wastewater with suspended solids, organic pollutants and ammonia nitrogen "three highs" in livestock and poultry breeding wastewater is the main source of ag...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C02F9/14C02F3/08C02F3/30C02F101/16C02F101/30
CPCC02F9/00C02F3/082C02F3/005C02F3/302C02F1/00C02F1/66C02F7/00C02F3/34C02F2101/16C02F2101/30Y02W10/10
Inventor 张千张小平郭青松张丽杰袁春波刘向阳赵天涛
Owner CHONGQING UNIV OF TECH
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