CN204824547U - Float formula river course purifier - Google Patents
Float formula river course purifier Download PDFInfo
- Publication number
- CN204824547U CN204824547U CN201520629585.3U CN201520629585U CN204824547U CN 204824547 U CN204824547 U CN 204824547U CN 201520629585 U CN201520629585 U CN 201520629585U CN 204824547 U CN204824547 U CN 204824547U
- Authority
- CN
- China
- Prior art keywords
- room
- aeration
- filler
- oil removal
- biochemical
- 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.)
- Expired - Fee Related
Links
- 238000005273 aeration Methods 0.000 claims abstract description 43
- 239000000945 filler Substances 0.000 claims abstract description 34
- 239000004576 sand Substances 0.000 claims abstract description 20
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 20
- 239000001301 oxygen Substances 0.000 claims description 20
- 229910052760 oxygen Inorganic materials 0.000 claims description 20
- 238000000746 purification Methods 0.000 claims description 18
- 239000000725 suspension Substances 0.000 claims description 9
- 238000007667 floating Methods 0.000 claims description 7
- 238000005452 bending Methods 0.000 claims description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 33
- 239000010865 sewage Substances 0.000 abstract description 23
- 230000006872 improvement Effects 0.000 abstract description 3
- 238000009434 installation Methods 0.000 abstract description 3
- 230000008901 benefit Effects 0.000 abstract description 2
- 210000005056 cell body Anatomy 0.000 abstract 3
- 238000006213 oxygenation reaction Methods 0.000 abstract 2
- 238000005188 flotation Methods 0.000 abstract 1
- 239000003643 water by type Substances 0.000 abstract 1
- 238000000034 method Methods 0.000 description 6
- 230000005484 gravity Effects 0.000 description 5
- 238000012423 maintenance Methods 0.000 description 5
- 230000000694 effects Effects 0.000 description 4
- 230000008569 process Effects 0.000 description 4
- 230000008859 change Effects 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 230000002906 microbiologic effect Effects 0.000 description 3
- 239000013049 sediment Substances 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 238000011109 contamination Methods 0.000 description 2
- 238000009413 insulation Methods 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 238000005192 partition Methods 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 230000001105 regulatory effect Effects 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 description 1
- 238000010170 biological method Methods 0.000 description 1
- 230000031018 biological processes and functions Effects 0.000 description 1
- 238000003763 carbonization Methods 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000012851 eutrophication Methods 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
- 231100001240 inorganic pollutant Toxicity 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 238000002203 pretreatment Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 230000008439 repair process Effects 0.000 description 1
- 238000009987 spinning Methods 0.000 description 1
- 210000002700 urine Anatomy 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
Landscapes
- Physical Water Treatments (AREA)
Abstract
The utility model discloses a float formula river course purifier, including the cell body, be equipped with the biochemical room of the sand setting room that connects gradually, oil removal room and aeration in the cell body, have a flotation pontoon with bolted connection respectively in the both sides of cell body, separate through the interception baffle between sand setting room and the oil removal room, oil removal room and aeration separate through the guide plate between the biochemical room, the top of the biochemical room of aeration is equipped with the roof, has placed the oxygenation pump on the roof, is equipped with soft filler and filler bracket in the centre of aeration biochemical room, and the bottom is equipped with the high current aeration pipe with oxygenation pump intercommunication, filler bracket is located the upper and lower both ends of soft filler. The device can carry out the preliminary treatment to all kinds of sewage that get into the river course, and through increasing the biochemical room of aeration, the demand that makes sewage each item index homoenergetic reach river course quality of water has high efficiency, compact structure, area is little, energy -conserving and convenient advantage is maintained in the installation, can extensively be applicable to the improvement of waters such as river course water, lake.
Description
Technical field
The utility model relates to a kind of waste disposal plant, particularly floatation type river channel purification plant.
Background technology
Along with five water are controlled and being rooted in the hearts of the people of sustainable development altogether, urban river water administers the attention causing society at leisure, traditional river regulation is waited until that river water quality becomes when eutrophication is serious on turn black smelly or river course exactly and is just drawn attention, and people just start to adopt physics and biological method to administer for river water body itself.Also have the water quality to entering river course to carry out pretreated, such as the food and drink waste water in kitchen at embedded underground water-and-oil separator, for the excrement and urine water of Public toilets etc. at embedded underground septic tank.But practice shows, qualified discharge is difficult to, suspended substance residual in sewage, chemical oxygen demand (COD) only according to these physics modes and the pretreated sanitary sewage of anaerobe mode, biochemical oxygen demand (BOD) index is still higher, enters the variation that neighbouring water body will inevitably cause water quality.
For this present situation, the utility model intends clean device these sanitary sewages more than the process of Drain contamination for river channel mouth adopting a kind of novelty, and adopting the mode of multi-stage type physical treatment and Aerobic biological process to improve processing efficiency to sewage, the water quality making to enter water body is limpid up to standard.
Utility model content
The purpose of this utility model provides a kind of for the process of river sewage mouth and the little floatation type river channel purification plant of floor space to solve above-mentioned the deficiencies in the prior art.
To achieve these goals, floatation type river channel purification plant designed by the utility model, comprise pond body, be provided with in the body of described pond connect successively sand setting room, oil removal room and aeration biochemical room, floating drum is connected with bolt respectively in the both sides of pond body, separate by tackling baffle plate between described sand setting room and oil removal room, separated by flow deflector between described oil removal room and aeration biochemical room, described interception baffle plate vertically arrange and its upper end near the direction bending of flow deflector, same described flow deflector vertically arrange and its lower end to the direction bending near interception baffle plate; The top of described aeration biochemical room is provided with top board, top board is placed with oxygen increasing pump, be provided with soft-filler and filler support in the centre of aeration biochemical room, bottom is provided with the high current aeration tube be communicated with oxygen increasing pump, and described filler support is positioned at the two ends up and down of soft-filler.
The macrobead inorganic sediment that described sand setting room is carried by gravity settling separation sewage.
Described oil removal room utilizes oil phase for the principle of water from heavy and light, by interception baffle plate, make the oleaginous materials in sewage and small granular suspended matters separated float on interception baffle plate above liquid level, sewage enters aeration biochemical room by the subsurface flow deflector in oil removal room.
Described aeration biochemical indoor location soft-filler, by upper and lower filler support, soft-filler is fixed on centre, oxygen increasing pump aeration simultaneously, and discharge small aeration bubbles by high current aeration tube, the aerobic microbiological be attached on filler utilizes these bubbles to carry out the carbonization of filling surface with the organism flowing through filler, the denitrification of nitrated and filler inside, make the contamination index in water, and organism and ammonia nitrogen obtains biochemical degradation.The soft-filler that described soft-filler is made up of biochemical sponge, utilize its specific surface area large, the feature that air water perviousness is good, attached microbial, carries out biochemical treatment to water body.
Be provided with the floating drum be bolted to connection in the both sides of pond body, by the buoyancy of floating drum, Chi Tike regulated according to water-level fluctuation, avoid urban river water flow backward in the body of pond and sewage in the body of pond is leaked in river course.
Conveniently install, the side of described pond body is run through union lever, and the two ends of union lever are provided with suspension ring.Described suspension ring can be connected with the rope on riverbank, fix under rope effect with bank, prevent pond body from wandering.Described union lever is used for the suspension ring at connection pool body two ends, and balancing tank body two ends rope is stressed.
For the ease of the maintenance of aeration biochemical room, change cleaned and changed soft-filler, the equipment of maintenance aeration biochemical indoor, described top board is provided with access cover.
The top of described oxygen increasing pump is provided with rain cover, in rain cover, be provided with louvre.This rain cover can immerse oxygen increasing pump by rainproof anti-river, again can sound insulation and noise reduction.
In concrete use procedure, the sewage of river course water port enters the sand setting room of pond body by flow by gravity, the macrobead inorganic sediment that sand setting room is carried by gravity settling separation sewage, by the pretreated sewage of sand setting again by the interception baffle plate in the middle of sand setting room and oil removal room, oleaginous materials in sewage and small granular suspended matters float over liquid level above baffle plate, and sewage enters aeration biochemical room by the subsurface flow deflector in oil removal room.Soft-filler is equipped with in aeration biochemical indoor, and in the effect of oxygen increasing pump aeration, the aerobic microbiological be attached on filler utilizes small aeration bubbles to flow through the oxidation operation degraded of filler, and final outflow water is up to standard enters river course.
The utility model, by the ingehious design to floatation type river channel purification plant internal structure, is compared with traditional river course treatment process, is had following feature:
1, this device single floatation type oil partition tank different from the past, oil partition tank can only play a part to exclude oil slick, can not effectively remove for organic and inorganic pollutant deliquescent in water.This device adds aeration biochemical room, makes spinning off from the pollution treatment in water body face of river regulation, changes the improvement to the several point source of pollution entered in river course into.From the treatment after pollution Mode change in river course be river water body uncontaminated before control models in advance.
2, this device can carry out advanced treatment to the septic tank in urban wastewater treatment and water-and-oil separator water outlet, improve water probability of meeting water quality standard, alleviate river course purification and dirty load of receiving, thus make river course only rely on the ability of the river self-purification just can maintain clear water matter.
3, this device is easy for installation, only need fix by the suspension ring rope on device and on the bank, and little to river course area occupied, can not affect the navigation of ship on river course.
4, device-adaptive is strong, relies on the buoyancy of floating drum, according to river water level automatic regulating device height, prevent in river immersion device, and the sewage in device can leak in the body of river.
5, plant running expense is low, and without other energy consumption equipment except small power oxygen increasing pump, and without the need to adding medicament in device, can automatically run after device connects electricity, the operations staff without the need to sole duty keeps an eye on, thus reduces working cost.
6, oxygen increasing pump adopts low noise motor, and is provided with rain cover outside oxygen increasing pump, has soundproof effect concurrently, can effectively anti-locking apparatus on the impact of surrounding environment.
7, turnaround of unit is convenient, and aeration biochemical room is provided with access cover, can open access cover keep in repair as overhauled by professional and technical personnel.Sand setting room and oil removal room are unlimited form, do not establish top board, only need regularly to drag for clearly sand setting room and oil removal room, cleaning oil slick and settling, can normally run by holdout device.
In sum, the floatation type river channel purification plant that the utility model obtains can carry out pre-treatment to all kinds of sewage entering river course, by increasing aeration biochemical room, make sewage indices all can reach the demand of river water quality, have efficient, compact construction, floor space are little, energy-conservation and installation and maintenance advantage easily, can be widely used in the improvement of the water body such as urban river water, lake.
Accompanying drawing explanation
Fig. 1 is the orthographic plan of the floatation type river channel purification plant of embodiment 1;
Fig. 2 is the sectional view of the floatation type river channel purification plant of embodiment 1;
Fig. 3 is the orthographic plan of the floatation type river channel purification plant of embodiment 2;
Fig. 4 is the structural representation of the floatation type river channel purification plant of embodiment 2.
In figure: pond body 1, sand setting room 2, oil removal room 3, aeration biochemical room 4, bolt 5, floating drum 6, interception baffle plate 7, flow deflector 8, top board 9, oxygen increasing pump 10, soft-filler 11, filler support 12, high current aeration tube 13, union lever 14, suspension ring 15, access cover 16, rain cover 17, louvre 18, rope 19.
Embodiment
Below in conjunction with drawings and Examples, the utility model is further illustrated.
Embodiment 1:
As Fig. 1, shown in Fig. 2, the floatation type river channel purification plant that the present embodiment provides, comprise pond body 1, it is characterized in that: in described pond body 1, be provided with the sand setting room 2 connected successively, oil removal room 3 and aeration biochemical room 4, floating drum 6 is connected with bolt 5 respectively in the both sides of pond body 1, separate by tackling baffle plate 7 between described sand setting room 2 and oil removal room 3, separated by flow deflector 8 between described oil removal room 3 and aeration biochemical room 4, described interception baffle plate 7 vertically arrange and its upper end to the direction bending near flow deflector 8, described flow deflector 8 also vertically arrange and its lower end to the direction bending near interception baffle plate 7, the top of described aeration biochemical room 4 is provided with top board 9, top board 9 is placed with oxygen increasing pump 10, be provided with soft-filler 11 and filler support 12 in the centre of aeration biochemical room 4, bottom is provided with the high current aeration tube 13 be communicated with oxygen increasing pump 10, and described filler support 12 is positioned at the two ends up and down of soft-filler 11.
For the ease of the maintenance of aeration biochemical room 4, change cleaned and changed soft-filler 11, the equipment in maintenance aeration biochemical room 4, described top board 9 is provided with access cover 16.
The top of described oxygen increasing pump 10 is provided with rain cover 17, is provided with louvre 18 in rain cover 17.This rain cover 17 can immerse oxygen increasing pump 10 by rainproof anti-river, again can sound insulation and noise reduction.
In concrete use procedure, the sewage of river course water port enters the sand setting room 2 of pond body by flow by gravity, the macrobead inorganic sediment that sand setting room 2 is carried by gravity settling separation sewage, by the pretreated sewage of sand setting again by the interception baffle plate 7 in the middle of sand setting room 2 and oil removal room 3, oleaginous materials in sewage and small granular suspended matters float over liquid level above baffle plate, and sewage enters aeration biochemical room 4 by the subsurface flow deflector 8 in oil removal room 3.Aeration biochemical room 4 is built with soft-filler 11, and in the effect of oxygen increasing pump 10 aeration, the aerobic microbiological be attached on soft-filler 11 utilizes small aeration bubbles to flow through the oxidation operation degraded of soft-filler 11, and final outflow water is up to standard enters river course.
Embodiment 2:
As shown in Figure 3, Figure 4, the floatation type river channel purification plant that the present embodiment provides, its general structure is identical with embodiment 1, but in specific implementation process, conveniently install, the side of described pond body 1 is run through union lever 14, and the two ends of union lever 14 are provided with suspension ring 15.Described suspension ring 15 can be connected with the rope 19 on riverbank, fix, prevent pond body 1 from wandering under rope 19 acts on bank.Described union lever 14 is for the suspension ring 15 at connection pool body 1 two ends, and balancing tank body 15 two ends rope is stressed.
Claims (4)
1. a floatation type river channel purification plant, comprise pond body (1), it is characterized in that: in described pond body (1), be provided with the sand setting room (2) connected successively, oil removal room (3) and aeration biochemical room (4), bolt (5) is used to be connected with floating drum (6) respectively in the both sides of pond body (1), separate by tackling baffle plate (7) between described sand setting room (2) and oil removal room (3), separated by flow deflector (8) between described oil removal room (3) and aeration biochemical room (4), described interception baffle plate (7) vertically arrange and its upper end to the direction bending near flow deflector (8), described flow deflector (8) also vertically arrange and its lower end to the direction bending near interception baffle plate (7), the top of described aeration biochemical room (4) is provided with top board (9), top board (9) is placed with oxygen increasing pump (10), soft-filler (11) and filler support (12) is provided with in the centre of aeration biochemical room (4), bottom is provided with the high current aeration tube (13) be communicated with oxygen increasing pump (10), and described filler support (12) is positioned at the two ends up and down of soft-filler (11).
2. floatation type river channel purification plant according to claim 1, is characterized in that: the side in described pond body (1) is run through union lever (14), and the two ends of union lever (14) are provided with suspension ring (15).
3. floatation type river channel purification plant according to claim 1 and 2, is characterized in that: described top board (9) is provided with access cover (16).
4. floatation type river channel purification plant according to claim 1 and 2, is characterized in that: the top of described oxygen increasing pump (10) is provided with rain cover (17), is provided with louvre (18) in rain cover (17).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201520629585.3U CN204824547U (en) | 2015-08-20 | 2015-08-20 | Float formula river course purifier |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201520629585.3U CN204824547U (en) | 2015-08-20 | 2015-08-20 | Float formula river course purifier |
Publications (1)
Publication Number | Publication Date |
---|---|
CN204824547U true CN204824547U (en) | 2015-12-02 |
Family
ID=54682168
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201520629585.3U Expired - Fee Related CN204824547U (en) | 2015-08-20 | 2015-08-20 | Float formula river course purifier |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN204824547U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108222214A (en) * | 2018-03-19 | 2018-06-29 | 宁波伊玛水环境科技有限公司 | Modular river regulation system |
-
2015
- 2015-08-20 CN CN201520629585.3U patent/CN204824547U/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108222214A (en) * | 2018-03-19 | 2018-06-29 | 宁波伊玛水环境科技有限公司 | Modular river regulation system |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN105731724B (en) | A kind of offshore platform life sewage treatment and reuse method with high salt | |
CN103936148A (en) | Constant-effluent variable-load SVBR sewage processing technology | |
CN105967438A (en) | Integrated system and process for treating domestic sewage of villages and towns | |
CN102718365A (en) | Buried sewage treatment device | |
CN108249691B (en) | Integrated low-energy-consumption distributed village and town domestic sewage treatment system | |
CN203112657U (en) | Constant-effluent variable-load SVBR (Steady outflow Variable load Biological Reactor) sewage treater | |
CN110790451A (en) | Black odorous water treatment system and method for treating black odorous water by using same | |
CN203048742U (en) | Novel rural domestic sewage treatment integrated device | |
CN111777178B (en) | Vertical oxidation ditch micro-power water treatment system | |
CN204824547U (en) | Float formula river course purifier | |
CN210340465U (en) | Novel SBR reaction tank | |
CN205556404U (en) | Offshore platform sewage treatment unit | |
CN209468279U (en) | A kind of country sewage solar wind-energy processing equipment | |
CN103183412A (en) | Biochemical treatment device for sewage and treatment method thereof | |
CN205856266U (en) | Large-scale integrated sewage treating apparatus | |
CN211570383U (en) | Sewage draining port water treatment equipment for urban drainage pipeline | |
CN202246338U (en) | Integrated rural sewage treatment device | |
CN112299654A (en) | Movable black smelly water treatment equipment | |
CN112028233A (en) | Solar-assisted aeration activated sludge tank | |
CN111977889A (en) | Landscape type urban domestic sewage ecological treatment system | |
CN110697973A (en) | Sewage draining port water treatment equipment for urban drainage pipeline | |
CN205528252U (en) | Take sewage treatment plant of auxiliary material automatic control function | |
CN2818472Y (en) | In situ composite reaction treater for domestic and fecal sewage | |
CN204824546U (en) | Contact oxidation sewage treatment plant | |
CN210736484U (en) | Household sewage treatment device |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C56 | Change in the name or address of the patentee | ||
CP03 | Change of name, title or address |
Address after: 315100 Zhejiang city in Ningbo Province, Yinzhou District Road No. 298 building (Bachelor of Zhejiang Tiandi Environmental Engineering Co. Ltd.) Patentee after: ZHEJIANG WORLD CLEAN ENVIRONMENT ENGINEERING Co.,Ltd. Address before: 315100 Zhejiang city of Ningbo province of Yinzhou District Road No. 270 building room 1408 (Bryan Ningbo Tiandi Environmental Engineering Co. Ltd.) Patentee before: NINGBO QINGTIANDI ENVIRONMENT ENGINEERING Co.,Ltd. |
|
CF01 | Termination of patent right due to non-payment of annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20151202 |