CN204874023U - Bury formula catalytic oxidation AO technology sewage treatment plant - Google Patents
Bury formula catalytic oxidation AO technology sewage treatment plant Download PDFInfo
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- CN204874023U CN204874023U CN201520600216.1U CN201520600216U CN204874023U CN 204874023 U CN204874023 U CN 204874023U CN 201520600216 U CN201520600216 U CN 201520600216U CN 204874023 U CN204874023 U CN 204874023U
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- pond
- catalytic oxidation
- aerobic pond
- contact aerobic
- pump
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- 230000003647 oxidation Effects 0.000 title claims abstract description 28
- 238000007254 oxidation reaction Methods 0.000 title claims abstract description 28
- 230000003197 catalytic Effects 0.000 title claims abstract description 26
- 239000010865 sewage Substances 0.000 title abstract description 13
- 238000005516 engineering process Methods 0.000 title abstract description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 53
- 238000004062 sedimentation Methods 0.000 claims abstract description 16
- 238000000746 purification Methods 0.000 claims abstract description 8
- 239000000945 filler Substances 0.000 claims abstract description 5
- 238000000034 method Methods 0.000 claims description 17
- 239000010802 sludge Substances 0.000 claims description 16
- 238000007599 discharging Methods 0.000 claims description 14
- 238000010992 reflux Methods 0.000 claims description 10
- 230000000630 rising Effects 0.000 claims description 7
- 229910052760 oxygen Inorganic materials 0.000 abstract description 12
- MYMOFIZGZYHOMD-UHFFFAOYSA-N oxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 abstract description 12
- 239000001301 oxygen Substances 0.000 abstract description 12
- 241000276438 Gadus morhua Species 0.000 abstract description 11
- 235000019516 cod Nutrition 0.000 abstract description 11
- 238000005273 aeration Methods 0.000 abstract description 3
- 238000005265 energy consumption Methods 0.000 abstract description 2
- 241000893018 Armeria Species 0.000 abstract 1
- 241000196324 Embryophyta Species 0.000 abstract 1
- 241000233866 Fungi Species 0.000 abstract 1
- 230000002349 favourable Effects 0.000 abstract 1
- 230000001546 nitrifying Effects 0.000 abstract 1
- 239000011259 mixed solution Substances 0.000 description 6
- 229910052698 phosphorus Inorganic materials 0.000 description 4
- 239000002028 Biomass Substances 0.000 description 3
- OAICVXFJPJFONN-UHFFFAOYSA-N phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 3
- 239000011574 phosphorus Substances 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 241000894006 Bacteria Species 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 230000001276 controlling effect Effects 0.000 description 2
- 235000014113 dietary fatty acids Nutrition 0.000 description 2
- 239000000194 fatty acid Substances 0.000 description 2
- 150000004665 fatty acids Chemical class 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000006228 supernatant Substances 0.000 description 2
- 230000037250 Clearance Effects 0.000 description 1
- 241000565118 Cordylophora caspia Species 0.000 description 1
- 206010061529 Polyp Diseases 0.000 description 1
- 230000035512 clearance Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 230000000813 microbial Effects 0.000 description 1
- 230000000050 nutritive Effects 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 230000001105 regulatory Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
Abstract
The utility model discloses a bury formula catalytic oxidation AO technology sewage treatment plant, including setting gradually first heavy pond, catch basin, equalizing basin, the integral type catalytic oxidation AO reactor below the earth's surface, one of them style catalytic oxidation AO reactor includes that the oxygen deficiency pond, the one -level that communicate have in proper order contacted the oxygen pond, the second grade has contacted oxygen pond, sedimentation tank, the equalizing basin passes through the diaphragm pump and links to each other with the oxygen deficiency pond, the one -level has contacted the upper portion that oxygen pond, second grade had contacted the oxygen pond and has been equipped with aeration systems to having contacted oxygen pond, second grade in the one -level and being equipped with three -dimensional elastic filler in having contacted the oxygen pond, one side of sedimentation tank is equipped with the water purification outlet pipe, and its bottom is equipped with the mud delivery pipe. The utility model discloses divide into the two -stage with the good oxygen section of traditional AO technology to be equipped with elastic space packing in the cell body, more be favorable to nitrifying the growth of fungus, guarantee getting rid of of COD and NH3+ -N, and the saving energy consumption, practice thrift area simultaneously, reduce running cost and initial investment.
Description
Technical field
The utility model relates to a kind of catalytic oxidation A/O process spent water treatment unit, particularly relates to a kind of buried catalytic oxidation A/O process spent water treatment unit, belongs to field of biological sewage treatment.
Background technology
Along with expanding economy, body eutrophication phenomenon is day by day serious.Body eutrophication is mainly caused by the existence of the nutritive substances such as N, P.Denitrogenation dephosphorizing has become the focus and emphasis of the research of sewage disposal in recent years.Current utilization is activated sludge process and biomembrance process denitrogenation dephosphorizing comparatively widely.But these traditional technologys often also exist, and floor space is large, operation process is complicated, the shortcoming of poor efficiency high energy consumption.
Utility model content
The purpose of this utility model is to problems of the prior art, provides a kind of buried catalytic oxidation A/O process spent water treatment unit.
Buried catalytic oxidation A/O process spent water treatment unit of the present utility model, comprises the preliminary sedimentation tank, water collecting basin, equalizing tank, the integral type catalytic oxidation A/O reactor that are successively set on below earth's surface; Wherein the side of preliminary sedimentation tank is provided with water inlet pipe, and opposite side top communicates with water collecting basin top; The bottom of preliminary sedimentation tank is provided with mud discharging pipe; Water collecting basin is connected by pipeline and lift pump with equalizing tank; Described integral type catalytic oxidation A/O reactor comprise be communicated with successively anoxic pond, one-level contact Aerobic Pond, Secondary contact Aerobic Pond, settling tank, described equalizing tank is connected with anoxic pond by surge pump; The built-in agitator of anoxic pond; The top of one-level contact Aerobic Pond, Secondary contact Aerobic Pond is provided with aerating system, and is provided with 3 D elastic filler in one-level contact Aerobic Pond, Secondary contact Aerobic Pond; The side of settling tank is provided with water purification rising pipe, is provided with mud discharging pipe bottom it.
Principle of work of the present utility model: sewage enters the suspended solid (by its base sludge delivery pipe discharged) of preliminary sedimentation tank in precipitation removal sewage, again through water collecting basin (collect and store sewage), then after equalizing tank (regulating the water quality and quantity of sewage), enter the anoxic pond of buried catalytic oxidation A/O reactor integratedly, in anoxic pond, oxygen bacterium and amphimicrobe utilize the voltaile fatty acid in former water fully to carry out anaerobic phosphorus release, and COD a large amount of in former water is removed; Organonitrogen in the simultaneous oxidation water that the COD of one-level contact Aerobic Pond to former water removes and NH
3 +-N; Secondary contact Aerobic Pond removes remaining COD and most NH
3 +-N, enters settling tank afterwards and carries out mud-water separation, and supernatant liquor is through the discharge of water purification rising pipe, and mud is discharged through settling tank base sludge delivery pipe.
Have constant microbial biomass to maintain in reactor, the mud discharging pipe of settling tank is connected with described anoxic pond by sludge reflux pump; Anoxic pond is connected with described Secondary contact Aerobic Pond by internal circulation pump.The nitrated mixed solution flowed out from Secondary contact Aerobic Pond is back to anoxic pond through internal circulation pump, and the reflux ratio of nitrated mixed solution is 200%-400%, fully carries out denitrification denitrogenation; Synchronously enter the mud also had through the backflow of sludge reflux pump autoprecipitation pond in anoxic pond, with the biomass of post-reactor, return sludge ratio is 50%-100%.
In described integral type catalytic oxidation A/O reactor, the bottom of anoxic pond to contact Aerobic Pond by water outlet bottom with one-level is communicated with, the top of one-level contact Aerobic Pond connects the bottom of Secondary contact Aerobic Pond by pipeline, the top of Secondary contact Aerobic Pond connects the bottom of settling tank by pipeline, the top of settling tank arranges water purification rising pipe.
The external air pump of described aerating system, to carry out aeration oxygen supply to one-level contact Aerobic Pond, Secondary contact Aerobic Pond.
For the ease of controlling, the mud discharging pipe in heavy pond, the mud discharging pipe of settling tank are equipped with control valve; The pipeline of lift pump, surge pump, internal circulation pump, sludge reflux pump both sides is equipped with control valve.
The utility model has the following advantages relative to prior art:
1, the aerobic section of traditional A/O technique is divided into two-stage by the utility model, and is provided with elastic solid filler in the body of pond, is more conducive to the growth of nitrifier, ensures COD and NH
3 +the removal of-N;
2, aerating system and sludge recirculation system are automatic control, achieve aeration oxygen supply to water quality and quantity adaptability, can energy efficient, reduce running cost and initial investment;
3, buried structure is adopted, floor space little (saving floor occupying area more than 30%), capital construction cost low (reducing by 30%), running cost low (reducing by 20%).
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Embodiment
Below in conjunction with Fig. 1, structure and working principle of the present utility model is described further.
A kind of buried catalytic oxidation A/O process spent water treatment unit, comprises the preliminary sedimentation tank 1, water collecting basin 2, equalizing tank 3, the integral type catalytic oxidation A/O reactor 15 that are successively set on below earth's surface.Wherein the side of preliminary sedimentation tank 1 is provided with water inlet pipe, and opposite side top communicates with water collecting basin 2 top; The bottom of preliminary sedimentation tank 1 is provided with mud discharging pipe.Water collecting basin 2 is connected by pipeline and lift pump 13 with equalizing tank 3.Integral type catalytic oxidation A/O reactor 15 comprise be communicated with successively anoxic pond 4, one-level contact Aerobic Pond 5, Secondary contact Aerobic Pond 6, settling tank 7; The bottom that wherein bottom of anoxic pond 4 to contact Aerobic Pond 5 by water outlet with one-level is communicated with, the top of one-level contact Aerobic Pond 5 connects the bottom of Secondary contact Aerobic Pond 6 by pipeline, the top of Secondary contact Aerobic Pond 6 connects the bottom of settling tank 7 by pipeline, the top of settling tank 7 arranges water purification rising pipe.Equalizing tank 3 is connected with anoxic pond 4 by surge pump 14; The built-in agitator 10 of anoxic pond 4; The top of one-level contact Aerobic Pond 5, Secondary contact Aerobic Pond 6 is provided with the aerating system 9 of external air pump 16, and is provided with 3 D elastic filler 8 in one-level contact Aerobic Pond 5, Secondary contact Aerobic Pond 6; The side of settling tank 7 is provided with water purification rising pipe, is provided with mud discharging pipe bottom it, and this mud delivery pipe is connected with described anoxic pond 4 by sludge reflux pump 12; Anoxic pond 4 is connected with described Secondary contact Aerobic Pond 6 by internal circulation pump 11.Above-mentioned each pond body is synthetic glass structure.
For the ease of controlling, the mud discharging pipe of the mud discharging pipe of preliminary sedimentation tank 1, settling tank 7 is equipped with control valve; The pipeline of lift pump 13, surge pump 14, internal circulation pump 11, sludge reflux pump 12 both sides is equipped with control valve.
During use, sewage enters the suspended solid of preliminary sedimentation tank 1 in primary deposition removal sewage, the mud of preliminary sedimentation tank 1 is discharged by its base sludge delivery pipe I, then equalizing tank 3 is entered through lift pump 13, the anoxic pond 4 of equalizing tank 3 water outlet in surge pump 14 enters buried catalytic oxidation A/O reactor 15 integratedly successively, one-level contact Aerobic Pond 5, Secondary contact Aerobic Pond 6, settling tank 7.Anerobe and amphimicrobe utilize the voltaile fatty acid in former water fully to carry out anaerobic phosphorus release in anoxic pond 4, in former water, the COD of 60% is removed, the nitrated mixed solution flowed out from Secondary contact Aerobic Pond 6 is back to anoxic pond 4 through internal circulation pump 11, the reflux ratio of nitrated mixed solution is 200%-400%, fully carries out denitrification denitrogenation; Mixed solution flows into one-level contact Aerobic Pond 5 from anoxic pond 4 afterwards, mainly carries out removing the organonitrogen in simultaneous oxidation water and NH to the COD of former water
3 +-N, in former water, the COD of about 30% is removed; Synchronously enter the mud also had through the backflow of sludge reflux pump 12 autoprecipitation pond 7 in anoxic pond 4, with the biomass of post-reactor, return sludge ratio is 50%-100%.The water outlet of one-level contact Aerobic Pond 5 enters Secondary contact Aerobic Pond 6, and Secondary contact Aerobic Pond 6 Main Function is for removing remaining COD and most NH
3 +-N, simultaneously absorbs the phosphorus in sewage two Aerobic Pond section polyP bacteria excess, and mixed solution enters settling tank 7 and carries out mud-water separation afterwards, and supernatant liquor discharges through pure water pipe, and mud is discharged through settling tank 7 base sludge delivery pipe IV.
This equipment is used for the process of town domestic sewage, its effluent quality can reach more than the one-level A standard in National Standard of the People's Republic of China's town domestic sewage treatment plant pollutant emission standard (GB18918-2002), and can energy efficient, reduce running cost and initial investment.Compared with traditional wastewater treatment unit, can realize capital construction cost and reduce by 30%, running cost reduces by 20% and saves floor occupying area more than 30%, its COD, NH simultaneously
3 +the clearance of-N, TN, TP is respectively 90%, 98%, 80%, 90%, water outlet COD, NH
3 +-N, TN, TP are less than 40mg/L, 1mg/L, 15mg/L, 0.5mg/L respectively.
Claims (6)
1. a buried catalytic oxidation A/O process spent water treatment unit, comprises the preliminary sedimentation tank (1), water collecting basin (2), equalizing tank (3), integral type catalytic oxidation A/O reactor (15) that are successively set on below earth's surface; Wherein the side of preliminary sedimentation tank (1) is provided with water inlet pipe, and opposite side top communicates with water collecting basin (2) top; The bottom of preliminary sedimentation tank (1) is provided with mud discharging pipe; Water collecting basin (2) is connected by pipeline and lift pump (13) with equalizing tank (3); It is characterized in that: described integral type catalytic oxidation A/O reactor (15) comprises the anoxic pond (4), one-level contact Aerobic Pond (5), Secondary contact Aerobic Pond (6), the settling tank (7) that are communicated with successively, and described equalizing tank (3) is connected with anoxic pond (4) by surge pump (14); Described anoxic pond (4) built-in agitator (10); The top of one-level contact Aerobic Pond (5), Secondary contact Aerobic Pond (6) is provided with aerating system (9), and is provided with 3 D elastic filler (8) in one-level contact Aerobic Pond (5), Secondary contact Aerobic Pond (6); The side of described settling tank (7) is provided with water purification rising pipe, is provided with mud discharging pipe bottom it.
2. buried catalytic oxidation A/O process spent water treatment unit as claimed in claim 1, is characterized in that: the mud discharging pipe of settling tank (7) is connected with described anoxic pond (4) by sludge reflux pump (12); Anoxic pond (4) is connected with described Secondary contact Aerobic Pond (6) by internal circulation pump (11).
3. buried catalytic oxidation A/O process spent water treatment unit as claimed in claim 1 or 2, it is characterized in that: in described integral type catalytic oxidation A/O reactor (15), the bottom of anoxic pond (4) to contact Aerobic Pond (5) by water outlet bottom with one-level is communicated with, the top of one-level contact Aerobic Pond (5) connects the bottom of Secondary contact Aerobic Pond (6) by pipeline, the top of Secondary contact Aerobic Pond (6) connects the bottom of settling tank (7) by pipeline, the top of settling tank (7) arranges water purification rising pipe.
4. buried catalytic oxidation A/O process spent water treatment unit as claimed in claim 1 or 2, is characterized in that: described aerating system (9) external air pump (16).
5. buried catalytic oxidation A/O process spent water treatment unit as claimed in claim 1 or 2, is characterized in that: the mud discharging pipe of described preliminary sedimentation tank (1), the mud discharging pipe of settling tank (7) are equipped with control valve.
6. buried catalytic oxidation A/O process spent water treatment unit as claimed in claim 1 or 2, is characterized in that: the pipeline of described lift pump (13), surge pump (14), internal circulation pump (11), sludge reflux pump (12) both sides is equipped with control valve.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520600216.1U CN204874023U (en) | 2015-08-11 | 2015-08-11 | Bury formula catalytic oxidation AO technology sewage treatment plant |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520600216.1U CN204874023U (en) | 2015-08-11 | 2015-08-11 | Bury formula catalytic oxidation AO technology sewage treatment plant |
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| Publication Number | Publication Date |
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| CN204874023U true CN204874023U (en) | 2015-12-16 |
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| CN201520600216.1U Active CN204874023U (en) | 2015-08-11 | 2015-08-11 | Bury formula catalytic oxidation AO technology sewage treatment plant |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110066831A (en) * | 2019-03-13 | 2019-07-30 | 杭州电子科技大学 | The quick natural pond method processed of kitchen garbage |
| CN110526398A (en) * | 2019-08-27 | 2019-12-03 | 南京环保产业创新中心有限公司 | A kind of micropollutant water treatment reactor and its method |
-
2015
- 2015-08-11 CN CN201520600216.1U patent/CN204874023U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110066831A (en) * | 2019-03-13 | 2019-07-30 | 杭州电子科技大学 | The quick natural pond method processed of kitchen garbage |
| CN110526398A (en) * | 2019-08-27 | 2019-12-03 | 南京环保产业创新中心有限公司 | A kind of micropollutant water treatment reactor and its method |
| CN110526398B (en) * | 2019-08-27 | 2022-03-08 | 南京环保产业创新中心有限公司 | Micro-polluted water treatment reactor and method thereof |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |