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Method for enhancing nitrogen and phosphorus removal of urban sewage by sludge fermentation

A technology for denitrification and dephosphorization and urban sewage, which is applied in the field of coupling control, can solve the problems of increasing the solid load of the treatment unit, difficulty in separation of mud and water, and difficulty in elutriation, so as to avoid slowing down the fermentation reaction rate, improve the removal effect of ammonia nitrogen, and strengthen the dehydration process. The effect of the nitrogen effect

Active Publication Date: 2014-03-26
北控水务(中国)投资有限公司
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Problems solved by technology

In actual engineering, if the fermentation-elution process is used to develop the composite carbon source in the sludge, there are some disadvantages: 1) Due to the adsorption of the sludge, the VFA produced by fermentation is difficult to be elutriated, and a higher However, the elutriation efficiency requires a large amount of elutriation water, and the elutriation efficiency is low, and the separation of mud and water is difficult; 2) it is difficult to avoid the occurrence of methane reaction in a completely anaerobic reactor, and the hydrolysis of particulate matter is a key factor for sludge anaerobic The rate-limiting step of aerobic fermentation, so the fermentation product is consumed by methanogens in large quantities; 3) In order to achieve high elutriation efficiency, a large amount of elutriation water is required, which will inevitably produce a large upward flow rate and bring out a lot of particulate matter , increasing the solid load of the subsequent processing unit

Method used

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  • Method for enhancing nitrogen and phosphorus removal of urban sewage by sludge fermentation

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Effect test

Embodiment 1

[0038] Sequencing batch reactor SBR 1 To treat domestic sewage with low C / N ratio, each cycle goes through 7 processes of water inflow, anoxic, water inflow, anaerobic, aeration, sedimentation, and drainage.

[0039] ⅠWater intake Set the water intake of the intake pump to 500ml / min, and the water intake lasts for 5 minutes. After the system is started, the sewage in the raw water tank enters the sequencing batch reactor SBR through the inlet pump 1 , open the first agitator while entering water.

[0040] Ⅱ Anoxic After the water inflow is completed, it enters the anoxic period, and the denitrification time is set to 30 minutes.

[0041] ⅢWater intake Set the water intake of the intake pump to 500ml / min, for 5 minutes.

[0042] Ⅳ Anaerobic After the second water inflow, it enters the anaerobic period. The phosphorus accumulating bacteria use the carbon source in the raw water to perform anaerobic phosphorus release. The time is set at 45 minutes.

[0043] Ⅴ Aeration Turn o...

Embodiment 2

[0055] Sequencing batch reactor SBR 1 To treat domestic sewage with low C / N ratio, each cycle goes through 7 processes of water inflow, anoxic, water inflow, anaerobic, aeration, sedimentation, and drainage.

[0056] ⅠWater intake Set the water intake of the intake pump to 1L / min, and the water intake takes 2.5 minutes. After the system is started, the sewage in the raw water tank enters the sequencing batch reactor SBR through the inlet pump 1 , open the first agitator while entering water.

[0057] Ⅱ Anoxic After the water inflow is completed, it enters the anoxic period, and the denitrification time is set to 30 minutes.

[0058] ⅢWater intake Set the water intake of the intake pump to 1L / min, and feed the water for 2.5 minutes.

[0059] Ⅳ Anaerobic After the second water inflow, it enters the anaerobic period. The phosphorus accumulating bacteria use the carbon source in the raw water to perform anaerobic phosphorus release. The time is set at 60 minutes.

[0060] Ⅴ Ae...

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Abstract

The invention discloses a method for enhancing nitrogen and phosphorus removal of urban sewage by sludge fermentation, relates to the coupling control technology of sludge fermentation enhanced nitrogen and phosphorus removal technology and sludge fermentation technology, and belongs to the fields of urban sewage treatment and sludge biochemical treatment. The method employs a sequencing batch reactor to couple the sludge fermentation effect and the urban sewage nitrogen and phosphorus removal effect into a same system, so that easily degradable carbon source generated by sewage fermentation can be consumed timely by phosphorus-accumulating bacterium and denitrifying bacterium, the nitrogen removal effect of the urban sewage with a low C / N ratio is enhanced, the problem of lowered fermentation reacting rate caused by accumulation of products in the fermentation process is avoided, and the initial stabilization of primary sludge is achieved at the same time. The method for enhancing nitrogen and phosphorus removal of urban sewage by sludge fermentation is applicable to the enhanced nitrogen and phosphorus removal of the urban sewage with low C / N ratio and C / P ratio and the initial decrement and stabilization of the sludge. The method for enhancing nitrogen and phosphorus removal of urban sewage by sludge fermentation is saving in carbon source and improved in nitrogen removal efficiency, and has the advantages of simple equipment, flexible operation, high nitrogen removal efficiency and the like.

Description

technical field [0001] The invention relates to a coupling control technology of an enhanced denitrification and phosphorus removal process of urban sewage and a sludge fermentation technology, and belongs to the fields of urban sewage treatment and sludge biochemical treatment. The process is suitable for the enhanced denitrification and dephosphorization of urban sewage with low C / N ratio and C / P ratio and the initial reduction and stabilization of sludge. Background technique [0002] my country's "Urban Sewage Treatment Plant Pollutant Discharge Standard" (GB18918-2002) promulgated in 2002 requires that the effluent water quality of all sewage units should be less than 50mg / L for COD, less than 5mg / L for ammonia nitrogen, less than 15mg / L for total nitrogen, and less than 15mg / L for total phosphorus. Less than 0.5mg / L (level A standard). COD emissions have been effectively controlled during the Eleventh Five-Year Plan period, but the issue of nitrogen and phosphorus emis...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C02F3/30C02F3/34
Inventor 彭永臻吴程程王淑莹张树军张亮操沈彬杜睿
Owner 北控水务(中国)投资有限公司
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