CN205347155U - Landfill leachate removes flavor system - Google Patents
Landfill leachate removes flavor system Download PDFInfo
- Publication number
- CN205347155U CN205347155U CN201620086685.0U CN201620086685U CN205347155U CN 205347155 U CN205347155 U CN 205347155U CN 201620086685 U CN201620086685 U CN 201620086685U CN 205347155 U CN205347155 U CN 205347155U
- Authority
- CN
- China
- Prior art keywords
- pond
- percolate
- sedimentation tank
- removal system
- packing layer
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
- 239000000149 chemical water pollutant Substances 0.000 title abstract description 4
- 239000000796 flavoring agent Substances 0.000 title abstract 2
- 235000019634 flavors Nutrition 0.000 title abstract 2
- 238000004062 sedimentation Methods 0.000 claims abstract description 20
- 238000012856 packing Methods 0.000 claims abstract description 13
- 238000005189 flocculation Methods 0.000 claims abstract description 12
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 11
- 230000016615 flocculation Effects 0.000 claims abstract description 11
- 239000001301 oxygen Substances 0.000 claims abstract description 11
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 11
- 238000004659 sterilization and disinfection Methods 0.000 claims abstract description 11
- 238000005273 aeration Methods 0.000 claims abstract description 8
- 238000001914 filtration Methods 0.000 claims abstract description 8
- 239000003513 alkali Substances 0.000 claims abstract description 6
- 230000001954 sterilising effect Effects 0.000 claims description 9
- 238000007599 discharging Methods 0.000 claims description 7
- 238000006297 dehydration reaction Methods 0.000 claims description 5
- 239000000706 filtrate Substances 0.000 claims description 5
- 238000011084 recovery Methods 0.000 claims description 5
- 239000002253 acid Substances 0.000 claims description 4
- 230000018044 dehydration Effects 0.000 claims description 4
- 239000000645 desinfectant Substances 0.000 claims description 3
- 239000011148 porous material Substances 0.000 claims description 3
- 239000007788 liquid Substances 0.000 abstract description 4
- 230000007613 environmental effect Effects 0.000 abstract description 3
- 238000004519 manufacturing process Methods 0.000 abstract description 3
- 239000007789 gas Substances 0.000 abstract 1
- 238000012805 post-processing Methods 0.000 abstract 1
- 239000000779 smoke Substances 0.000 abstract 1
- 238000005406 washing Methods 0.000 abstract 1
- 238000000034 method Methods 0.000 description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 8
- 239000003344 environmental pollutant Substances 0.000 description 4
- 231100000719 pollutant Toxicity 0.000 description 4
- 239000010865 sewage Substances 0.000 description 4
- 238000013461 design Methods 0.000 description 3
- 230000001105 regulatory effect Effects 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 2
- 230000007547 defect Effects 0.000 description 2
- 230000007812 deficiency Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000004134 energy conservation Methods 0.000 description 2
- 239000000945 filler Substances 0.000 description 2
- 229910001385 heavy metal Inorganic materials 0.000 description 2
- 239000010802 sludge Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000006228 supernatant Substances 0.000 description 2
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 description 1
- 239000003181 biological factor Substances 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000010841 municipal wastewater Substances 0.000 description 1
- 238000006213 oxygenation reaction Methods 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 239000002352 surface water Substances 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Abstract
The utility model discloses a landfill leachate removes flavor system, including the storage tank of placing filtration liquid, the export of storage tank links up the sedimentation tank through the grid, the sedimentation tank is through combined governing pond rank pH equalizing basin, the top in combined governing pond is provided with alkali and throws with the hole, the top of pH equalizing basin is provided with sour throwing with the hole, the exit of pH equalizing basin has set gradually oxygen debt pond, the anaerobism pond, good oxygen pond, the inside in good oxygen pond is provided with the aeration pipe, the fan that good oxygen pond top set up links up the gas pocket of aeration tube -surface, good oxygen pond top is provided with not filter relapses filterable back flow completely, the exit in good oxygen pond links up the flocculation basin, the disinfection pond is connected to the flocculation basin through the filtering pond, the inside packing layer that is provided with of filtering ponds, mud quantity when having reduced aerobic treatment among the anaerobic reactor, mud post processing's cost has been practiced thrift, landfill leachate's discharge to reach standard has been realized, reducing production cost, energy -conserving environmental protection again is a fine innovation scheme, the double -motor disassembling -and -washing -free smoke ventilator has a very good market prospect.
Description
Technical field
This utility model taste removal field, particularly relates to percolate taste removal system.
Background technology
Percolate is the sewage that a kind of high concentration, high toxic, composition are extremely complex, water quality along with region, living habit, economic level different very different.Pollutants from landfill leachate mainly has following source: great amount of soluble Organic substance, inorganic matter that rubbish itself contains dissolve in rainwater, surface water or subsoil water immersion process and enter percolate, rubbish enters percolate by the solable matter that the effects such as biology, chemistry, physics produce, and covers and enter in the soil of surrounding the solable matter of percolate.
Percolate is the product that liquid flows at landfill yard gravity, is mainly derived from the interior moisture of precipitation and rubbish itself.Owing to liquid has many factors to be likely to have influence on the character of percolate in flow process, including physical factor, chemical factor and biological factor etc., so the character of percolate changes in a sizable scope.In general, its pH value between 4～9, COD in the scope of 2000～62000mg/L, BOD5 from 60～45000mg/L, heavy metal concentration and in municipal wastewater the concentration of heavy metal basically identical.Percolated liquid in city refuse landfill is the high concentrated organic wastewater of a kind of complicated component, is directly discharged into environment if untreated, can cause serious environmental pollution.To protect for the purpose of environment, percolate is carried out process is requisite, but the water outlet that existing process device processes is difficult to qualified discharge.
In sum, for the defect of prior art, it is accordingly required in particular to percolate taste removal system, to solve the deficiencies in the prior art.
Utility model content
Deficiency in processing for percolate of the prior art, causes the severe contamination to environment, the utility model proposes percolate taste removal system; novel in design; achieve the qualified discharge of percolate, environment is had good protective effect, has solved the defect of prior art.
To achieve these goals, the technical solution of the utility model is as follows:
Percolate taste removal system, including the storage tank placing percolate, the outlet of storage tank is connected sedimentation tank through grid, sedimentation tank is by rank pH regulator pond, comprehensive adjustment pond, the top in comprehensive adjustment pond is provided with alkali and adds hole, the top in pH regulator pond is provided with acid and adds hole, the exit in pH regulator pond is disposed with oxygen debt pond, anaerobic pond, Aerobic Pond, Aerobic Pond be internally provided with aeration tube, the pore on the blower fan linking aeration tube surface that Aerobic Pond top is arranged, Aerobic Pond top is provided with does not filter the return duct repeatedly filtered completely, the exit linking flocculation basin of Aerobic Pond, flocculation basin connects sterilization pool through filter tank, filtering ponds are internally provided with packing layer.
Further, the top of described flocculation basin is provided with automatic feeder.
Further, described pH regulator pond and the lower section of Aerobic Pond are provided with mud discharging pipe, mud discharging pipe linking electrolyzer, and electrolyzer connects Sedimentation tank, the dehydration pond that Sedimentation tank linking mud is deposited.
Surface configuration at sterilization pool described in the utility model has disinfectant solution inlet hole, and sterilization pool is connected filtrate recovery pond through effusion meter.
Further, described packing layer adopts and puts honeycomb inclined-tube packing layer or cobblestone packing layer.
The beneficial effects of the utility model are: reasonable in design, coordinative composition of equipments is good, ensure that the sewage upflow velocity in anaerobic reactor, decrease the supernatant in sedimentation tank and be back to the consumption of anaerobic reactor, 50% of excess sludge in sedimentation tank is made to enter anaerobic reactor, reduce mud consumption during Aerobic Process for Treatment in anaerobic reactor, save the cost of mud later stage process, achieve the qualified discharge of percolate, reduce production cost, energy-conservation environmental protection again is a kind of well innovation scheme, has very much marketing prospect.
Accompanying drawing explanation
This utility model is described in detail below in conjunction with the drawings and specific embodiments:
Fig. 1 is structural representation of the present utility model.
100-storage tank in figure, 110-grid, 120-sedimentation tank, 130-comprehensive adjustment pond, 131-alkali adds hole, 140-pH regulating reservoir, and 141-acid adds hole, 150-is oxygen debt pond, 160-anaerobic pond, 170-Aerobic Pond, 180-electrolyzer, 190-Sedimentation tank, 200-dehydration pond, 210-flocculation basin, 220-filtering ponds, 230-sterilization pool, 240-filtrate recovery pond, 250-return duct, 260-mud discharging pipe, 270-blower fan.
Detailed description of the invention
For the technological means making this utility model realize, creation characteristic, reach purpose and effect and be easy to understand, below in conjunction with being specifically illustrating, this utility model is expanded on further.
Referring to Fig. 1, percolate taste removal system, including the storage tank 100 placing percolate, the outlet of storage tank 100 is connected sedimentation tank 120 through grid 110, sedimentation tank 120 holds in the mouth pH regulator pond 140 by comprehensive adjustment pond 130, the top in comprehensive adjustment pond 130 is provided with alkali and adds hole 131, the top in pH regulator pond 140 is provided with acid and adds hole 141, the exit in pH regulator pond 140 is disposed with oxygen debt pond 150, anaerobic pond 160, Aerobic Pond 170, Aerobic Pond 170 be internally provided with aeration tube, the blower fan 270 that Aerobic Pond 170 top is arranged is connected the pore on aeration tube surface, Aerobic Pond 170 top is provided with does not filter the return duct 250 repeatedly filtered completely, the exit linking flocculation basin 210 of Aerobic Pond 170, flocculation basin 210 connects sterilization pool 230 through filtering ponds 220, filtering ponds 220 are internally provided with packing layer.
It addition, the top of flocculation basin 210 is provided with automatic feeder.The lower section of pH regulator pond 140 and Aerobic Pond 170 is provided with mud discharging pipe 260, and mud discharging pipe 260 is connected electrolyzer 180, and electrolyzer 180 connects Sedimentation tank 190, and Sedimentation tank 190 is connected the dehydration pond 200 that mud is deposited.The surface configuration of sterilization pool 230 has disinfectant solution inlet hole, and sterilization pool 230 is connected filtrate recovery pond 240 through effusion meter.Packing layer adopts and puts honeycomb inclined-tube packing layer or cobblestone packing layer.
Percolate intercepts after bigger float through grid, enter the comprehensive adjustment pond regulating water quality water yield, add alkali at this and regulate percolate pH=11, remove most ammonia-nitrogen, enter pH regulator pond, after regulating pH=8, it is lifted into oxygen debt pond by pump, anaerobic pond, Aerobic Pond, make a return journey the pollutant in dewatering by relying on the biomembrane of apposition growth on filler, equipment removes the function of pollutant mainly in aerobic room, by air pump constantly toward aerobic zone oxygenation, the microorganism of apposition growth on aerobic filler is made to be in active state, constantly remove the pollutant in water, and finally make sewage curved limpid, ensure stable water outlet qualified discharge, mud enters into dehydration pond by electrolyzer, finally mud is carried out landfill disposal, it is recycled to the water in filtrate recovery pond can utilize, Practical Performance is excellent.
The beneficial effects of the utility model are: reasonable in design, coordinative composition of equipments is good, ensure that the sewage upflow velocity in anaerobic reactor, decrease the supernatant in sedimentation tank and be back to the consumption of anaerobic reactor, 50% of excess sludge in sedimentation tank is made to enter anaerobic reactor, reduce mud consumption during Aerobic Process for Treatment in anaerobic reactor, save the cost of mud later stage process, achieve the qualified discharge of percolate, reduce production cost, energy-conservation environmental protection again is a kind of well innovation scheme, has very much marketing prospect.
Skilled person will appreciate that of the industry; this utility model is not restricted to the described embodiments; described in above-described embodiment and description is that principle of the present utility model is described; under the premise without departing from this utility model spirit and scope, this utility model also has various changes and modifications, and these changes and improvements both fall within the scope of claimed this utility model.This utility model claims scope and is defined by appending claims and equivalent thereof.
Claims (5)
1. percolate taste removal system, including the storage tank placing percolate, it is characterized in that: the outlet of storage tank is connected sedimentation tank through grid, sedimentation tank is by rank pH regulator pond, comprehensive adjustment pond, the top in comprehensive adjustment pond is provided with alkali and adds hole, the top in pH regulator pond is provided with acid and adds hole, the exit in pH regulator pond is disposed with oxygen debt pond, anaerobic pond, Aerobic Pond, Aerobic Pond be internally provided with aeration tube, the pore on the blower fan linking aeration tube surface that Aerobic Pond top is arranged, Aerobic Pond top is provided with does not filter the return duct repeatedly filtered completely, the exit linking flocculation basin of Aerobic Pond, flocculation basin connects sterilization pool through filter tank, filtering ponds are internally provided with packing layer.
2. percolate taste removal system according to claim 1, it is characterised in that: the top of described flocculation basin is provided with automatic feeder.
3. percolate taste removal system according to claim 1, it is characterized in that: described pH regulator pond and the lower section of Aerobic Pond are provided with mud discharging pipe, mud discharging pipe linking electrolyzer, electrolyzer connects Sedimentation tank, the dehydration pond that Sedimentation tank linking mud is deposited.
4. percolate taste removal system according to claim 1, it is characterised in that: the surface configuration of described sterilization pool has disinfectant solution inlet hole, and sterilization pool is connected filtrate recovery pond through effusion meter.
5. percolate taste removal system according to claim 1, it is characterised in that: described packing layer adopts and puts honeycomb inclined-tube packing layer or cobblestone packing layer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620086685.0U CN205347155U (en) | 2016-01-25 | 2016-01-25 | Landfill leachate removes flavor system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620086685.0U CN205347155U (en) | 2016-01-25 | 2016-01-25 | Landfill leachate removes flavor system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205347155U true CN205347155U (en) | 2016-06-29 |
Family
ID=56184115
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620086685.0U Active CN205347155U (en) | 2016-01-25 | 2016-01-25 | Landfill leachate removes flavor system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205347155U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110510789A (en) * | 2019-09-10 | 2019-11-29 | 吕慧 | A kind of Domestic waste penetrating fluid purification device |
| CN117164177A (en) * | 2023-11-02 | 2023-12-05 | 珙县华洁危险废物治理有限责任公司成都分公司 | Biochemical treatment system and method for brewing wastewater |
-
2016
- 2016-01-25 CN CN201620086685.0U patent/CN205347155U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110510789A (en) * | 2019-09-10 | 2019-11-29 | 吕慧 | A kind of Domestic waste penetrating fluid purification device |
| CN117164177A (en) * | 2023-11-02 | 2023-12-05 | 珙县华洁危险废物治理有限责任公司成都分公司 | Biochemical treatment system and method for brewing wastewater |
| CN117164177B (en) * | 2023-11-02 | 2024-01-05 | 珙县华洁危险废物治理有限责任公司成都分公司 | Biochemical treatment system and method for brewing wastewater |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101898854B (en) | Method and device for treatment of high-sulfur content and low-permeability oil reservoir produced wastewater | |
| CN104310714B (en) | A kind of cultivation and system and technique thereof of butchering sewage processed | |
| CN203768124U (en) | Ecological filter for micro-polluted water treatment | |
| CN106082562B (en) | Community sewage integrated treatment and reuse system and application | |
| CN204474503U (en) | A kind of country sewage drips the ecological canal treatment system of filter | |
| CN204550325U (en) | Sewage from oil refinery treatment system | |
| CN104787958A (en) | Culturing farm sewage treatment system, and sewage treatment method | |
| CN210656590U (en) | Buried rural domestic sewage treatment system | |
| CN111362406A (en) | Suspended solar integrated water purification equipment and water purification method | |
| CN205347155U (en) | Landfill leachate removes flavor system | |
| CN203976581U (en) | The former enhanced water pretreatment unit in a kind of micro-polluted drinking water water source | |
| CN203360228U (en) | Tobacco wastewater treatment system | |
| CN206447733U (en) | A kind of oil-containing sewage treatment system | |
| CN211339184U (en) | Domestic sewage integrated treatment equipment based on steel slag ceramsite filler biological filter | |
| CN105254130A (en) | Wetland sewage treatment system and method thereof | |
| CN203284289U (en) | Combined electrode horizontal subsurface flow wet land device for efficient nitrogen removing of domestic sewage | |
| CN107117771A (en) | A kind of aquaculture wastewater joint processing system and its method | |
| CN106045202A (en) | Efficient low-energy-consumption biological landscape sewage treatment device and method | |
| CN105693016A (en) | Rain/sewage-mixed-flow-state river course distributed treatment technique | |
| CN206266401U (en) | A kind of integrated sewage treating apparatus | |
| CN106986506B (en) | Integrated industrial water purifier | |
| CN205676333U (en) | A kind of system utilizing artificial wetland treatment slaughterhouse sewage | |
| CN108793600A (en) | A kind of industrial, life combined sewage processing method | |
| CN210764857U (en) | Distributed rural domestic sewage treatment system | |
| CN209493370U (en) | A kind of integral bio trickling filter |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP03 | Change of name, title or address | ||
| CP03 | Change of name, title or address |
Address after: 321001 Zhuma Industrial Zone, Wucheng District, Jinhua City, Zhejiang Province Patentee after: Zhejiang Anke Environmental Protection Technology Co.,Ltd. Address before: 321000 Zhuma Industrial Zone, Wucheng District, Jinhua City, Zhejiang Province Patentee before: ZHEJIANG ANKE ENVIRONMENTAL PROTECTION TECHNOLOGY CO.,LTD. |
|
| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: Garbage leachate deodorization system Effective date of registration: 20231202 Granted publication date: 20160629 Pledgee: Zhejiang Jinhua Chengtai Rural Commercial Bank Co.,Ltd. Pledgor: Zhejiang Anke Environmental Protection Technology Co.,Ltd. Registration number: Y2023330002868 |