CN205061799U - Sewage multilevel processing device - Google Patents
Sewage multilevel processing device Download PDFInfo
- Publication number
- CN205061799U CN205061799U CN201520704512.6U CN201520704512U CN205061799U CN 205061799 U CN205061799 U CN 205061799U CN 201520704512 U CN201520704512 U CN 201520704512U CN 205061799 U CN205061799 U CN 205061799U
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- CN
- China
- Prior art keywords
- sludge
- tank
- sewage
- connecting pipe
- treatment chamber
- 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
- 239000010865 sewage Substances 0.000 title claims abstract description 33
- 238000012545 processing Methods 0.000 title abstract description 5
- 239000010802 sludge Substances 0.000 claims abstract description 37
- 238000011282 treatment Methods 0.000 claims abstract description 36
- 238000002955 isolation Methods 0.000 claims abstract description 34
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 19
- 238000001914 filtration Methods 0.000 claims abstract description 16
- 230000002906 microbiologic effect Effects 0.000 claims abstract description 15
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 14
- 238000000746 purification Methods 0.000 claims description 7
- 238000000926 separation method Methods 0.000 claims description 7
- 239000000377 silicon dioxide Substances 0.000 claims description 7
- 239000002245 particle Substances 0.000 claims description 5
- 238000000034 method Methods 0.000 abstract description 3
- 230000008569 process Effects 0.000 abstract description 3
- 239000010842 industrial wastewater Substances 0.000 abstract description 2
- 238000004065 wastewater treatment Methods 0.000 abstract description 2
- 238000004062 sedimentation Methods 0.000 abstract 8
- 244000005700 microbiome Species 0.000 abstract 3
- 230000008719 thickening Effects 0.000 abstract 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract 2
- 229910052760 oxygen Inorganic materials 0.000 abstract 2
- 239000001301 oxygen Substances 0.000 abstract 2
- 238000004064 recycling Methods 0.000 abstract 1
- 239000007788 liquid Substances 0.000 description 3
- 239000013618 particulate matter Substances 0.000 description 3
- 238000001556 precipitation Methods 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000002244 precipitate Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 230000009471 action Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 239000013043 chemical agent Substances 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- -1 meanwhile Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 244000052769 pathogen Species 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Landscapes
- Treatment Of Sludge (AREA)
Abstract
The utility model discloses a sewage multilevel processing device, including isolation tank, first dirty water sedimentation pond, the dirty water sedimentation pond of second, anaerobic microorganisms process chamber, good oxygen microbiological treatment room, sludge thickening jar and sludge press filtration room, the isolation tank right side is passed through communicating pipe and is connected first dirty water sedimentation pond, communicating pipe and the dirty water sedimentation pond of second intercommunication are passed through to first dirty water sedimentation pond, communicating pipe and anaerobic microorganisms process chamber intercommunication are passed through to the dirty water sedimentation pond of second, anaerobic microorganisms passes through the room communicating pipe and good oxygen microbiological treatment room intercommunication, the bottom in the dirty water sedimentation pond of first dirty water sedimentation pond and second all is connected with the sludge pump and connects the sludge thickening jar through the sludge pump, one side of sludge thickening jar is connected with the mud screw pump and connects the sludge press filtration room through the mud screw pump, the utility model discloses with industrial wastewater treatment and microbiological treatment tie mutually with, to sewage multilevel processing, the sewage after make handling reaches emission standard or the standard of recycling.
Description
Technical field
The utility model relates to technical field of sewage, particularly relates to a kind of sewage multi-stage treatment units.
Background technology
In the production and life of the mankind; the generation of sewage is inevitable; in recent years; along with the high speed development of science and technology and the rapid advances of society; the generation of sewage is also raising year by year; and these sewage mostly number be all unprocessed rivers,lakes and seas or the earth's surface of directly entering, so not only contaminate environment, and greatly waste water resources.
At present, along with people are for the pay attention to day by day of environmental problem, the associated processing device of sewage also increases, but current waste disposal plant only just filters and precipitation through simple, and is processed by pharmaceutical chemicals, and the sewage after such processing scheme not only makes process is difficult to be up to state standards, the use of chemical agent simultaneously also may increase secondary pollution, Given this, be necessary design one waste disposal plant more efficiently, solve current Problems existing successively.
Utility model content
The purpose of this utility model is just to provide a kind of sewage multi-stage treatment units to solve the problem, and effectively can solve drying materials and the problem such as production efficiency is lower.
In order to solve the problem, the utility model provides a kind of technical scheme: a kind of sewage multi-stage treatment units, comprise isolation tank, first detention tank, second detention tank, anaerobion treatment chamber, aerobic microbiological treatment chamber, sludge concentrating pot and sludge press filtration room, described isolation tank inside is divided into three isolation tanks by three road separation net grid, be respectively scum silica frost isolation tank, macrobead thing isolation tank and small particle isolation tank, sewage inlet pipe is connected on the left of described isolation tank, the first detention tank is connected by connecting pipe on the right side of described isolation tank, described first detention tank is communicated with the second detention tank by connecting pipe, described second detention tank is communicated with anaerobion treatment chamber by connecting pipe, described anaerobion treatment chamber is communicated with aerobic microbiological treatment chamber by connecting pipe, one side bottom of described aerobic microbiological treatment chamber is provided with water purification row mouth, described first detention tank is all connected with sludge pump with the bottom of the second detention tank and is connected sludge concentrating pot by sludge pump, the side of described sludge concentrating pot is connected with mud spiral pump and connects sludge press filtration room by mud spiral pump, one end of described sludge press filtration room is provided with mud row mouth, bottom is provided with drainage row mouth.
As preferably, the mesh diameter on described separation net grid reduces from left to right successively.
As preferably, described drainage row mouth is communicated with the first mudpan by connecting pipe.
As preferably, described sewage inlet pipe, connecting pipe and water purification row mouth is provided with valve.
The beneficial effects of the utility model: adopt multiple-stage treatment scheme, first scum silica frost, bulk particulate matter and fritter particulate matter is isolated, then repeatedly precipitate, and upper water liquid is carried out microbiological treatment, mud is carried out compressing and press filtration, combined with Industrial Waste Water Treatments by biology, sewage is reached and again utilizes standard or emission standard.
Accompanying drawing explanation
For ease of illustrating, the utility model is described in detail by following concrete enforcement and accompanying drawing.
Fig. 1 is structural representation of the present utility model.
1-isolation tank; 2-separation net grid; 3-scum silica frost isolation tank; 4-macrobead thing isolation tank; 5-small particle isolation tank; 6-sewage inlet pipe; 7-connecting pipe; 8-first detention tank; 9-second detention tank; 10-anaerobion treatment chamber; 11-aerobic microbiological treatment chamber; 12-water purification row mouth; 13-sludge pump; 14-sludge concentrating pot; 15-mud spiral pump; 16-sludge press filtration room; 17-mud row mouth; 18-drainage row mouth; 19-valve.
Embodiment
As shown in Figure 1, this embodiment is by the following technical solutions: a kind of sewage multi-stage treatment units, comprise isolation tank 1, first detention tank 8, second detention tank 9, anaerobion treatment chamber 10, aerobic microbiological treatment chamber 11, sludge concentrating pot 14 and sludge press filtration room 16, described isolation tank 1 inside is divided into three isolation tanks by three road separation net grid 2, be respectively scum silica frost isolation tank 3, macrobead thing isolation tank 4 and small particle isolation tank 5, sewage inlet pipe 6 is connected on the left of described isolation tank 1, the first detention tank 8 is connected by connecting pipe 7 on the right side of described isolation tank 1, described first detention tank 8 is communicated with the second detention tank 9 by connecting pipe 7, described second detention tank 9 is communicated with anaerobion treatment chamber 10 by connecting pipe 7, described anaerobion treatment chamber 10 is communicated with aerobic microbiological treatment chamber 11 by connecting pipe 7, one side bottom of described aerobic microbiological treatment chamber 11 is provided with water purification row mouth 12, described first detention tank 8 is all connected with sludge pump 13 with the bottom of the second detention tank 9 and is connected sludge concentrating pot 14 by sludge pump 13, the side of described sludge concentrating pot 14 is connected with mud spiral pump 15 and connects sludge press filtration room 16 by mud spiral pump 15, one end of described sludge press filtration room 16 is provided with mud row mouth 17, bottom is provided with drainage row mouth 18.
Wherein, the mesh diameter on described separation net grid 2 reduces from left to right successively; Described drainage row mouth 18 is communicated with the first mudpan 8 by connecting pipe 7; Described sewage inlet pipe 6, connecting pipe 7 and water purification row mouth 12 is provided with valve 19.
Concrete principle, during work, sewage enters isolation tank 1 through sewage inlet pipe 6, and successively by scum silica frost isolation tank 3, macrobead thing isolation tank 4 and small particle isolation tank 5 are respectively except the scum silica frost in decontaminated water, macrobead thing and the particulate matter that disappears, then sewage enters the first detention tank precipitation 8, after precipitation, upper water liquid is drawn into the second detention tank 9 by connecting pipe 7, upper water liquid in second detention tank 9 is drawn into anaerobion treatment chamber 10 by connecting pipe 7, promote the growth of anerobe by oxygen-free environment and decompose the partial organic substances in sewage by anerobe, then sewage enters aerobic microbiological treatment chamber 11, by oxidation, reduction and fermentative action, further decomposing organic matter, suppress the peculiar smell killed various harmful levels of pathogens and eliminate in sewage, meanwhile, mud bottom first detention tank 8 and the second detention tank 9 is by sludge pump 13 suction sludge concentrating pot 14, then by mud spiral pump 15, concentrated mud is pushed in sludge press filtration room 16, clod through press filtration is discharged from mud row mouth 17, the drainage of press filtration is introduced the first mudpan 8 again precipitate by being arranged with drainage connecting pipe 7 that mouth 18 is connected.
The technician more than shown and describe ultimate principle of the present utility model and principal character and the advantage industry of the present utility model should understand; the utility model is not restricted to the described embodiments; what describe in above-described embodiment and specification sheets just illustrates principle of the present utility model; under the prerequisite not departing from the utility model spirit and scope; the utility model also has various changes and modifications; these changes and improvements all fall within the scope of claimed the utility model, and the claimed scope of the utility model is defined by appending claims and equivalent thereof.
Claims (4)
1. a sewage multi-stage treatment units, it is characterized in that, comprise isolation tank (1), first detention tank (8), second detention tank (9), anaerobion treatment chamber (10), aerobic microbiological treatment chamber (11), sludge concentrating pot (14) and sludge press filtration room (16), described isolation tank (1) inside is divided into three isolation tanks by three roads separation net grid (2), be respectively scum silica frost isolation tank (3), macrobead thing isolation tank (4) and small particle isolation tank (5), described isolation tank (1) left side connects sewage inlet pipe (6), described isolation tank (1) right side connects the first detention tank (8) by connecting pipe (7), described first detention tank (8) is communicated with the second detention tank (9) by connecting pipe (7), described second detention tank (9) is communicated with anaerobion treatment chamber (10) by connecting pipe (7), described anaerobion treatment chamber (10) is communicated with aerobic microbiological treatment chamber (11) by connecting pipe (7), one side bottom of described aerobic microbiological treatment chamber (11) is provided with water purification row's mouth (12), described first detention tank (8) is all connected with sludge pump (13) with the bottom of the second detention tank (9) and is connected sludge concentrating pot (14) by sludge pump (13), the side of described sludge concentrating pot (14) is connected with mud spiral pump (15) and connects sludge press filtration room (16) by mud spiral pump (15), one end of described sludge press filtration room (16) is provided with mud row's mouth (17), bottom is provided with drainage row's mouth (18).
2. a kind of sewage multi-stage treatment units according to claim 1, is characterized in that: the mesh diameter on described separation net grid (2) reduces from left to right successively.
3. a kind of sewage multi-stage treatment units according to claim 1, is characterized in that: described drainage row's mouth (18) is communicated with the first mudpan (8) by connecting pipe (7).
4. a kind of sewage multi-stage treatment units according to claim 1, is characterized in that, described sewage inlet pipe (6), connecting pipe (7) and water purification row's mouth (12) are provided with valve (19).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520704512.6U CN205061799U (en) | 2015-09-12 | 2015-09-12 | Sewage multilevel processing device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520704512.6U CN205061799U (en) | 2015-09-12 | 2015-09-12 | Sewage multilevel processing device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205061799U true CN205061799U (en) | 2016-03-02 |
Family
ID=55388380
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520704512.6U Expired - Fee Related CN205061799U (en) | 2015-09-12 | 2015-09-12 | Sewage multilevel processing device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205061799U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107311399A (en) * | 2017-08-03 | 2017-11-03 | 王嘉宁 | A kind of Full-automatic purification device for chemical experiment waste liquid |
| CN109987807A (en) * | 2019-04-30 | 2019-07-09 | 生态环境部华南环境科学研究所 | A kind of innoxious ecological treatment apparatus of the smelly Sediments of urban black |
-
2015
- 2015-09-12 CN CN201520704512.6U patent/CN205061799U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107311399A (en) * | 2017-08-03 | 2017-11-03 | 王嘉宁 | A kind of Full-automatic purification device for chemical experiment waste liquid |
| CN107311399B (en) * | 2017-08-03 | 2020-11-06 | 山东合创环保科技有限公司 | Full-automatic purification device for chemical experiment waste liquid |
| CN109987807A (en) * | 2019-04-30 | 2019-07-09 | 生态环境部华南环境科学研究所 | A kind of innoxious ecological treatment apparatus of the smelly Sediments of urban black |
| CN109987807B (en) * | 2019-04-30 | 2022-04-12 | 生态环境部华南环境科学研究所 | Harmless ecological treatment device for bottom mud of urban black and odorous water body |
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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: 20160302 Termination date: 20170912 |
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| CF01 | Termination of patent right due to non-payment of annual fee |