CN205575874U - Processing apparatus of thermal power plant's waste water - Google Patents
Processing apparatus of thermal power plant's waste water Download PDFInfo
- Publication number
- CN205575874U CN205575874U CN201620198366.9U CN201620198366U CN205575874U CN 205575874 U CN205575874 U CN 205575874U CN 201620198366 U CN201620198366 U CN 201620198366U CN 205575874 U CN205575874 U CN 205575874U
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- waste water
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- processing means
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- engine plant
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Abstract
The utility model discloses a processing apparatus of thermal power plant's waste water, including and being connected the equalizing basin with the grid, the oil skimming pond is connected to the equalizing basin, and contact oxidation tank is connected in the oil skimming pond, and contact oxidation tank connects the sedimentation tank, and the tow filter is connected to the sedimentation tank, and the disinfection pond is connected to the tow filter. The utility model discloses filtering waste water after the residue after organic matter removal, nitrogen, phosphorus are removed to biomembrane catalytic oxidation method, getting rid of meticulous residue through high -efficient tow filter again through the sedimentation tank, can reach the retrieval and utilization standard after the disinfection, the water charging system of power plant can be got back to once more to the waste water after this device is handled, the emission of reduction sewage, improvement resource retrieval and utilization.
Description
[technical field]
This utility model belongs to field of waste water treatment, is specifically related to the processing means of a kind of waste water of heat-engine plant.
[background technology]
Thermal power plant is not only and is used water rich and influential family, is also blowdown rich and influential family simultaneously.According to statistics, the annual draining in thermal power plant accounts for the 10% of whole nation industrial undertaking discharge capacity.Although the concentration of pollutant is the highest, but owing to its discharge capacity is big so that total amount of pollutants discharged is huge, thus the most serious to the pollution level of environment.The waste water in thermal power plant mainly include industrial wastewater, oily waste water, containing coal waste water and sanitary sewage.Industrial wastewater major pollutants have float, oil, Organic substance and sulfide etc., and this kind of waste water enters receiving water body will cause different environmental pollutions, causes ecological disruption.
But during existing Technology is more directly to regulate pH, remove residue roughly, or fine filtering can not turn again to the water charging system of power plant the most again after bio-oxidation pond, it is unfavorable for the protection of environmental conservation and water resource.
[utility model content]
The purpose of this utility model is to overcome above-mentioned deficiency, it is provided that the processing means of a kind of waste water of heat-engine plant, enables the waste water after process to turn again to the water charging system of power plant, reduces the discharge of sewage, improves resource reusing.
In order to achieve the above object, this utility model includes being connected regulating reservoir with grid, and regulating reservoir connects oil skimming pond, and oil skimming pond connects contact-oxidation pool, and contact-oxidation pool connects sedimentation tank, and sedimentation tank connects fiber bundle filter, and fiber bundle filter connects sterilization pool.
Described contact-oxidation pool includes being placed in the perforation water-locator that bottom is connected with oil skimming pond, is placed in the film reaction district above perforation water-locator, and perforation water-locator and film reaction interval are provided with Aeration tank, and film reaction is provided with filler in district.
Described Aeration tank connects Aeration fan, is provided with aeration effusion meter between Aeration tank and Aeration fan.
Described grid connects sump, and sump connects regulating reservoir.
Described sump connects regulating reservoir by elevator pump.
Described sterilization pool offers feeding opening.
Described sedimentation tank connects sludge concentration tank, and sludge concentration tank connects mechanical dehydration pond, and the waste liquid outlet in mechanical dehydration pond connects regulating reservoir.
Described mechanical dehydration pond uses belt squeezing pressure filter.
Described fiber bundle filter uses molecule polypropylene fibre bundle as filtering material.
Described sedimentation tank is vertical sedimentation basin.
Compared with prior art, this utility model by after waste water filtering residue after microbe films osculation oxygenation method organics removal, nitrogen, phosphorus, fine residue is removed further through high-efficiency fiber bundle filter through sedimentation tank, reuse standard is can reach after sterilized, waste water after this device processes can turn again to the water charging system of power plant, reduce the discharge of sewage, improve resource reusing rate.
Further, the waste liquid outlet in this utility model mechanical dehydration pond connects regulating reservoir, it is possible to recycling waste liquid, saves resource.
Further, fiber bundle filter of the present utility model uses molecule polypropylene fibre bundle as filtering material, the most several up to tens microns microns of its filtrate diameter, reach micron order, relative to particulate filter, it is big that fiber bundle media has specific surface area, and the advantages such as filtration resistance is little solve the filtering accuracy of particulate filter by problems such as particle diameter of filter medium are limited.
Further, vertical sedimentation basin selected by sedimentation tank of the present utility model, and spoil disposal is convenient, and floor space is less.
[accompanying drawing explanation]
Fig. 1 is structural representation of the present utility model.
[detailed description of the invention]
Below in conjunction with the accompanying drawings this utility model is described further.
See Fig. 1, this utility model includes being connected regulating reservoir 4 with grid 1, sump 2 it is provided with between grid 1 and regulating reservoir 4, sump 2 connects regulating reservoir 4 by elevator pump 3, regulating reservoir 4 connects oil skimming pond 5, oil skimming pond 5 connects contact-oxidation pool 6, contact-oxidation pool 6 connects sedimentation tank 13, sedimentation tank 13 connects fiber bundle filter 14 and sludge concentration tank 17, sludge concentration tank 17 connects mechanical dehydration pond 18, the waste liquid outlet in mechanical dehydration pond 18 connects regulating reservoir 4, and fiber bundle filter 14 connects sterilization pool 16, and sterilization pool 16 offers feeding opening 15.
Contact-oxidation pool 6 includes being placed in the perforation water-locator 7 that bottom is connected with oil skimming pond 5, it is placed in the film reaction district 10 above perforation water-locator 7, it is provided with Aeration tank 8 between perforation water-locator 7 and film reaction district 10, filler 9 it is provided with in film reaction district 10, Aeration tank 8 connects Aeration fan 12, is provided with aeration effusion meter 11 between Aeration tank 8 and Aeration fan 12.
Preferably, mechanical dehydration pond 18 uses belt to squeeze pressure filter, and fiber bundle filter 14 uses molecule polypropylene fibre bundle to be vertical sedimentation basin as filtering material, sedimentation tank 13.
Method of work of the present utility model, comprises the following steps
Step one, sewage carries out pretreatment, and grid 1 is used for retaining larger particles float；
Step 2, the sewage after step one processes then enters regulating reservoir 4, and regulating reservoir 4 can improve biological treatment structures service condition, effectively regulates water quality, the water yield, pH, it is simple to subsequent treatment；
Step 3, the sewage after step 2 processes carries out oil skimming pond 5 oil removal and processes, effectively reduces the COD of biological treatment；
Step 4, the sewage after step 3 processes enters two stage treatment, carries out biological oxidation in biological contact oxidation pond, and major part Organic substance is removed in degraded, can also effectively remove phosphorus, nitrogen simultaneously；
Step 5, the sewage after step 4 processes carries out entering sedimentation tank 13 through biological oxidation waste water, and sedimentation tank 13 is in order to clarify mixed liquor and to concentrate activated sludge, so that sewage is purified；
Step 6, the mud after step 5 processes is through sludge concentration tank 17, and supernatant after mechanical dehydration is reflowable to be recycled to regulating reservoir, sludge cake outward transport landfill or be used as fertilizer；
Step 7, the sewage after step 5 processes removes less microgranule through fiber bundle filter 14 again, and sewage after process enters sterilization pool 16 and carries out disinfection, and finally reaches reuse standard.
Being provided with filler 9 in contact-oxidation pool 6, part microorganism is grown on filling surface with biomembranous form set, and part is then that cotton-shaped suspension growth is in water.With aerator aeration aerating bottom filler；Air can be from bottom to top, carry pending waste water secretly, passing freely through filtrate part and arrive ground, after air runaway, waste water then from up to down returns at the bottom of pond at filtrate layout, thus reduce the content of BOD, COD, activated sludge is attached to filling surface, does not flows with water, because of biomembrane directly by the strong agitation of ascending air, constantly update, thus improve clean-up effect.Biofilm development is to after certain thickness, the microorganism of nearly filler wall will carry out anaerobic metabolism due to anoxia, thus remove a large amount of nitrogen, phosphorus in water, the souring that the gas produced and aeration are formed can cause biomembranous coming off, and promote the growth of nascent membrane, forming biomembranous metabolism, the biomembrane come off will flow out outside pond with water outlet.
Claims (10)
1. the processing means of a waste water of heat-engine plant, it is characterized in that: include being connected regulating reservoir (4) with grid (1), regulating reservoir (4) connects oil skimming pond (5), oil skimming pond (5) connects contact-oxidation pool (6), contact-oxidation pool (6) connects sedimentation tank (13), sedimentation tank (13) connects fiber bundle filter (14), and fiber bundle filter (14) connects sterilization pool (16).
The processing means of a kind of waste water of heat-engine plant the most according to claim 1, it is characterized in that: described contact-oxidation pool (6) includes being placed in the perforation water-locator (7) that bottom is connected with oil skimming pond (5), it is placed in the film reaction district (10) of perforation water-locator (7) top, it is provided with Aeration tank (8) between perforation water-locator (7) and film reaction district (10), in film reaction district (10), is provided with filler (9).
The processing means of a kind of waste water of heat-engine plant the most according to claim 2, it is characterized in that: described Aeration tank (8) connects Aeration fan (12), is provided with aeration effusion meter (11) between Aeration tank (8) and Aeration fan (12).
The processing means of a kind of waste water of heat-engine plant the most according to claim 1, it is characterised in that: described grid (1) connects sump (2), and sump (2) connects regulating reservoir (4).
The processing means of a kind of waste water of heat-engine plant the most according to claim 4, it is characterised in that: described sump (2) connects regulating reservoir (4) by elevator pump (3).
The processing means of a kind of waste water of heat-engine plant the most according to claim 1, it is characterised in that: described sterilization pool (16) offers feeding opening (15).
The processing means of a kind of waste water of heat-engine plant the most according to claim 1, it is characterized in that: described sedimentation tank (13) connects sludge concentration tank (17), sludge concentration tank (17) connects mechanical dehydration pond (18), and the waste liquid outlet of mechanical dehydration pond (18) connects regulating reservoir (4).
The processing means of a kind of waste water of heat-engine plant the most according to claim 7, it is characterised in that: described mechanical dehydration pond (18) uses belt squeezing pressure filter.
The processing means of a kind of waste water of heat-engine plant the most according to claim 1, it is characterised in that: described fiber bundle filter (14) uses molecule polypropylene fibre bundle as filtering material.
The processing means of a kind of waste water of heat-engine plant the most according to claim 1, it is characterised in that: described sedimentation tank (13) is vertical sedimentation basin.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620198366.9U CN205575874U (en) | 2016-03-15 | 2016-03-15 | Processing apparatus of thermal power plant's waste water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620198366.9U CN205575874U (en) | 2016-03-15 | 2016-03-15 | Processing apparatus of thermal power plant's waste water |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205575874U true CN205575874U (en) | 2016-09-14 |
Family
ID=56868269
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620198366.9U Expired - Fee Related CN205575874U (en) | 2016-03-15 | 2016-03-15 | Processing apparatus of thermal power plant's waste water |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205575874U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109095711A (en) * | 2018-08-20 | 2018-12-28 | 邵金容 | A kind of industrial waste water of thermal power station can fully degraded processing unit and processing method |
-
2016
- 2016-03-15 CN CN201620198366.9U patent/CN205575874U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109095711A (en) * | 2018-08-20 | 2018-12-28 | 邵金容 | A kind of industrial waste water of thermal power station can fully degraded processing unit and processing method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160914 Termination date: 20170315 |
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| CF01 | Termination of patent right due to non-payment of annual fee |