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Kitchen waste fermentation wastewater treatment device

A technology for fermenting waste water and kitchen waste, applied in the direction of backflow water treatment, multi-stage water treatment, water/sewage treatment, etc., can solve the problems of high operating cost, blockage of reverse osmosis membrane, unsatisfactory, etc., to avoid frequent cleaning, Effective denitrification and improvement of operating efficiency

Inactive Publication Date: 2017-11-03
CHINA MACHINERY INT ENG DESIGN & RES INST
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The waste water is treated successively through the adjustment tank of the oil separation primary sedimentation tank, the first pH adjustment tank, the ammonia stripping tower, the second pH adjustment tank, the A / O biochemical treatment device, the sedimentation tank, the Fenton reactor, and the coagulation sedimentation tank. In the removal of COD, BOD in wastewater 5 , SS and other pollutants at the same time, it can effectively remove TN, TP and effectively reduce the chroma of wastewater, and improve the removal rate of TN and TP. COD and BOD in the treated wastewater 5 , TN, NH 3 - N, TP, chroma and other pollutants can stably meet the "Comprehensive Discharge Standard for Sewage" (GB8978-1996) "Three-Class Standard" and "Water Quality Standard for Sewage Discharged into Urban Sewers" (GB / T 31962-2015) "B It has good effect, but it does not meet the requirements of "Class I Standard" of "Integrated Wastewater Discharge Standard" (GB8978-1996)
[0005] In the prior art, there is also a treatment device composed of "pretreatment device + anaerobic treatment device + aerobic treatment device + reverse osmosis membrane filtration device". High, especially the anaerobic treatment device consumes the carbon source in the wastewater during operation, which further reduces the carbon-nitrogen ratio in the wastewater (COD, BOD 5 lower ammonia nitrogen), the lower carbon-nitrogen ratio is not conducive to the biological denitrification of wastewater; the second is that the reverse osmosis membrane filtration device is used as the advanced treatment at the end, although it can meet the "B level" of the "Water Quality Standards for Sewage Discharge into Urban Sewers" The requirements of the standard and the "Class I Standard" of the "Comprehensive Wastewater Discharge Standard" (GB8978-1996) are insufficient. The grease in the wastewater can easily cause the reverse osmosis membrane to be blocked, and the high salt in the wastewater will accelerate the aging of the reverse osmosis membrane. The service life of the reverse osmosis membrane is short, especially the reverse osmosis membrane filtration device is a physical filtration device, which only intercepts the pollutants in the wastewater, but does not really degrade the pollutants. The large amount of concentrated liquid produced needs to be processed separately. The treatment of the process is easy to cause secondary pollution, and the operating cost is high

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specific Embodiment approach

[0023] See the attached picture for a treatment scale of 100m 3 / d of kitchen waste wastewater as an example, the specific implementation is as follows:

[0024] Wastewater after anaerobic digestion and dehydration of food waste slurry and waste water produced in other processes of food waste treatment Water quality: COD: 12000-15000mg / L, BOD 5 : 4500~5000mg / L, TN: 2100~2400mg / L, NH 3 -N: 1800~2000mg / L, TP: 110~130mg / L, SS: 7000~10000mg / L, animal and vegetable oil: 800~1000mg / L, pH: 7.5~8, chromaticity: 800~1000 times.

[0025] Referring to the accompanying drawings, the present invention includes an oil separation primary sedimentation tank 1, a regulating tank 2, an A / O biochemical treatment device 3, a sedimentation tank 4, a first coagulation sedimentation tank 5, a Fenton reactor 6, and a second coagulation sedimentation tank 7. Biological aerated filter 8;

[0026] The oil-separating primary sedimentation tank 1 has an oil slick baffle 1a on the top, a sludge chamber ...

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Abstract

The invention discloses a kitchen waste fermentation wastewater treatment device, and relates to wastewater treatment devices after anaerobic digestion and dehydration on kitchen waste paste. Wastewater is treated by an oil removal primary settling tank (1), a regulating reservoir (2), an A / O biochemical treatment device (3), a sedimentation basin (4), a first coagulating sedimentation tank (5), a Fenton reactor (6), a second coagulating sedimentation tank (7) and a biological aerated filter (8) in sequence; while pollutants such as COD (chemical oxygen demand), BOD5 and SS (suspended solid) in the wastewater are effectively removed, TN (total nitrogen) and TP (total phosphorus) can be effectively removed, wastewater chroma can be effectively lowered, and TN and TP removal rates can be effectively increased, and the pollutants such as the COD, the BOD5, NH3-N, the TP and the chroma in the treated wastewater can stably meet the requirement of level 1 standard in Integrated wastewater discharge standard (GB8978-1996).

Description

technical field [0001] The invention belongs to a treatment device for kitchen waste fermentation wastewater, in particular to a treatment device for waste water after anaerobic digestion and dehydration of kitchen waste slurry and waste water produced in other processes of kitchen waste treatment, and belongs to the field of sewage treatment. Background technique [0002] Wastewater after anaerobic digestion and dehydration of food waste slurry, as well as waste water generated by other processes of food waste treatment, has complex components and is a high-concentration organic wastewater that is difficult to treat. The concentration of pollutants in wastewater is high, chemical oxygen demand (COD, 8000-20000mg / L), BOD 5 (4000~8000mg / L), total nitrogen (TN, 2000~3000mg / L), ammonia nitrogen (NH 3 -N, 1500~2500mg / L), total phosphorus (TP, 50~150mg / L), suspended solids (SS, >8000mg / L), salt content (15000~30000mg / L), animal and vegetable oil (800~1500mg / L), chromaticity...

Claims

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Application Information

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IPC IPC(8): C02F9/14
CPCC02F9/00C02F1/40C02F1/5281C02F1/66C02F1/722C02F3/02C02F3/301C02F3/302C02F2001/007C02F2301/04C02F2301/08C02F2303/04C02F2305/026
Inventor 蒋剑虹罗友元唐清畅
Owner CHINA MACHINERY INT ENG DESIGN & RES INST
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