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Enhanced sewage biological nitrogen and phosphorus removal method bases on polyhydroxyalkanoate metabolism regulation

A polyhydroxyalkanoate and sewage technology, applied in biological sludge treatment, chemical instruments and methods, biological water/sewage treatment, etc., can solve the problem of low carbon source concentration, difficult treatment of greenhouse gas primary and secondary sedimentation sludge and other issues, to achieve the effects of improving efficiency, easy large-scale promotion, and low cost of process transformation

Active Publication Date: 2015-01-14
TONGJI UNIV +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, on the one hand, this method will cause greenhouse gas emissions and a large amount of primary and secondary sedimentation sludge is difficult to deal with; on the other hand, urban sewage generally has the problem of low carbon source concentration, and the low carbon-nitrogen ratio of sewage is difficult. Meet the increasing requirements of phosphorus and nitrogen removal

Method used

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  • Enhanced sewage biological nitrogen and phosphorus removal method bases on polyhydroxyalkanoate metabolism regulation

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0036] (1) if figure 1 As shown, the organic waste obtained by the sewage through the grid 1, the regulating tank 2 and the primary sedimentation tank 3 and the remaining sludge of the secondary sedimentation tank 5 are introduced into the sludge thickening tank 6 for concentration and sedimentation for 24 hours at a VSS ratio of 1:1;

[0037] (2) The concentrated mixture enters the PHA precursor production reactor 9 (anaerobic fermentation for 8 days under the condition of controlling pH=10.0) and is directional converted into PHA precursor;

[0038] (3) The obtained PHA precursor (concentration is 4650mg COD / L, the contents of acetic acid and propionic acid are 48% and 41% respectively) enters the sludge dehydrator 12 after removing nitrogen and phosphorus in the sludge conditioning tank 10, and the obtained liquid pumps Enter the PHA precursor storage pool 11 for storage;

[0039] (4) Pump the liquid in the supernatant storage tank 7 and the PHA precursor into the PHA prod...

Embodiment 2

[0042] (1) if figure 1 As shown, the organic waste obtained by the sewage through the grid 1, the regulating tank 2 and the primary sedimentation tank 3 and the remaining sludge of the secondary sedimentation tank 5 are introduced into the sludge concentration tank 6 for concentration and precipitation for 12 hours at a VSS ratio of 10:1;

[0043] (2) The concentrated mixture enters the PHA precursor production reactor 9 (anaerobic fermentation under the condition of controlling pH=8.0 for 8 days);

[0044](3) The obtained PHA precursor (concentration is 4230mg COD / L, the contents of acetic acid and propionic acid are 56% and 28% respectively) enters the sludge dehydrator 12 after removing nitrogen and phosphorus in the sludge conditioning tank 10, and the obtained liquid pumps Enter the PHA precursor storage pool 11 for storage;

[0045] (4) Pump the liquid in the supernatant storage tank 7 and the PHA precursor into the PHA production reactor 8 (control pH=6.8, react for 3....

Embodiment 3

[0047] (1) if figure 1 As shown, the organic waste obtained by the sewage through the grid 1, the regulating tank 2 and the primary sedimentation tank 3 and the remaining sludge of the secondary sedimentation tank 5 are introduced into the sludge concentration tank 6 for concentration and precipitation for 24 hours at a VSS ratio of 5:1;

[0048] (2) The concentrated mixture enters the PHA precursor production reactor 9 (anaerobic fermentation under the condition of controlling pH=8 for 8 days);

[0049] (3) The obtained PHA precursor (concentration is 4310mg COD / L, the contents of acetic acid and propionic acid are 50% and 31% respectively) enters the sludge dehydrator 12 after removing nitrogen and phosphorus in the sludge conditioning tank 10, and the obtained liquid pumps Enter the PHA precursor storage pool 11 for storage;

[0050] (4) Pump the liquid in the supernatant storage tank 7 and the PHA precursor into the PHA production reactor 8 (control pH=7.2, react for 3.5 ...

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Abstract

An enhanced sewage biological nitrogen and phosphorus removal method based on polyhydroxyalkanoates metabolic regulation, the method comprising the following steps: 1) passing the sewage through a primary sedimentation tank (3) to obtain granular organic substance, and importing the obtained granular organic substance together with the surplus sludge discharged from a secondary sedimentation tank (5) into a sludge thickening tank (6) for thickening; 2) anaerobically fermenting the thickened organic waste obtained from step 1) in a polyhydroxyalkanoates precursor production reactor (9) to synthesize a polyhydroxyalkanoates precursor; 3) after removing nitrogen and phosphorus from the anaerobically fermented mixture in a sludge conditioning tank (10), pumping the liquid into a polyhydroxyalkanoates precursor storage tank (11); 4) pumping the polyhydroxyalkanoates precursor into the polyhydroxyalkanoates production reactor (9) to produce polyhydroxyalkanoates; 5) pumping the polyhydroxyalkanoates produced in step 4) into a sewage biological nitrogen and phosphorus removal reactor (4) for nitrogen and phosphorus removal. The method increases the nitrogen and phosphorus removal rate to around 80% and 95%, and enables the effluent discharged after sewage treatment to meet the first level standard A of the sewage discharge standards, and also has advantages of easy process control, less production of greenhouse gas and sludge, and low transformation process cost, and the like.

Description

technical field [0001] The invention belongs to the technical field of biological treatment of water, waste water or sewage, and relates to a method for enhancing phosphorus and nitrogen removal of urban sewage by regulating the metabolism of polyhydroxyalkanoate (PHA) by an in-situ carbon source. Background technique [0002] With the development of the economy and the improvement of living standards, the discharge of industrial and domestic sewage has increased year by year, and the problem of water pollution has become increasingly serious. A large amount of nutrients such as nitrogen and phosphorus flow into natural water bodies such as rivers and lakes, resulting in widespread eutrophication. The discharge of nitrogen and phosphorus in sewage is the main cause of water eutrophication. Activated sludge method has become a main method for removing nitrogen and phosphorus in sewage because of its advantages such as easy operation. However, on the one hand, this method wi...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C02F9/14
CPCC02F3/308C02F11/02C02F11/04C12P7/625Y02W10/20
Inventor 陈银广郑雄任洪强苏应龙唐诗璟
Owner TONGJI UNIV
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