CN106865765A - A kind of vertical microkinetic self-loopa efficient sewage treatment installation - Google Patents
A kind of vertical microkinetic self-loopa efficient sewage treatment installation Download PDFInfo
- Publication number
- CN106865765A CN106865765A CN201710128890.8A CN201710128890A CN106865765A CN 106865765 A CN106865765 A CN 106865765A CN 201710128890 A CN201710128890 A CN 201710128890A CN 106865765 A CN106865765 A CN 106865765A
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- China
- Prior art keywords
- cylinder
- bucket
- sewage treatment
- inlet pipe
- water inlet
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Classifications
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/30—Aerobic and anaerobic processes
- C02F3/301—Aerobic and anaerobic treatment in the same reactor
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2203/00—Apparatus and plants for the biological treatment of water, waste water or sewage
- C02F2203/006—Apparatus and plants for the biological treatment of water, waste water or sewage details of construction, e.g. specially adapted seals, modules, connections
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Abstract
The invention discloses a kind of vertical microkinetic self-loopa efficient sewage treatment installation, it is related to technical field of sewage treatment equipment, including processing equipment body, the processing equipment body includes base plate and the cylinder on base plate, anaerobic zone is provided with the cylinder, oxygen consumption area and anoxic zone, the anoxic zone includes inner cylinder, water inlet pipe is provided with the inner cylinder, the water inlet pipe is communicated with the outside through cylinder, water inlet tube end is provided with sewage inlet port, the oxygen consumption area includes petal type eddy flow cloth bucket, bucket and baffler, the anaerobic zone is located between cylinder and inner cylinder, it is low the invention provides one kind power consumption, space availability ratio is high, vertical microkinetic self-loopa efficient sewage treatment installation rational in infrastructure.
Description
Technical field
The present invention relates to technical field of sewage treatment equipment, and in particular at a kind of vertical microkinetic self-loopa high-efficiency sewage
Reason equipment.
Background technology：
Sewage disposal is generally made up of Physical, chemical method, physical-chemical process and the big series of biochemical process four, is mostly
Be only possible to complete whole sewage disposal process by two or more method, its equipment based on building construction, machine
Based on unit cell supplemented by electric equipment, floor space is there is greatly, investment is high, and operating cost is high, and anti-load-bearing capacity is poor, reaction
Efficiency is low, management is compared with the problem for falling behind, device efficiency is low.A similar work is continued to use in treatment to sewage at present always
Skill route, such as traditional activated sludge process, develop into A/O techniques and A2/O techniques, are substantially the increase in and detest (scarce) oxygen biological treatment
With detest (scarce) oxygen pond, traditional A2/0 or the equipment of inversion A 2/0, its anaerobic zone, anoxic zone, oxygen consumption area are that formula arrangement of lying (is appreciated that
It is anaerobic zone, anoxic zone, the equal determinants area in oxygen consumption area), and each area need to scramble dynamic (or stirring) device, so that mud is not
Deposition, floor space is larger and power consumption is higher, therefore, design a kind of efficient sewage treatment installation that can solve the problem that problem above
Become problem demanding prompt solution.
The content of the invention
It is an object of the invention to provide a kind of vertical microkinetic self-loopa efficient sewage treatment installation, to solve existing skill
Caused above-mentioned multinomial defect in art.
A kind of vertical microkinetic self-loopa efficient sewage treatment installation, including processing equipment body, the processing equipment sheet
Body includes base plate and the cylinder on base plate, and anaerobic zone, oxygen consumption area and anoxic zone, the anoxic zone are provided with the cylinder
Including inner cylinder, water inlet pipe is provided with the inner cylinder, the water inlet pipe is communicated with the outside through cylinder, water inlet tube end is provided with dirt
Water inlet port, the oxygen consumption area includes petal type eddy flow cloth bucket, bucket and baffler, and the petal type eddy flow cloth bucket is located at
Inner cylinder top, the bucket is connected with baffler, and air inlet pipe, one end of the air inlet pipe are provided with petal type eddy flow cloth bucket
It is communicated with the outside, air inlet tube end is provided with air inlet, the anaerobic zone is located between cylinder and inner cylinder, and eddy flow is provided with outside inner cylinder
Water distributor, the cylinder top is provided with central tube, and the position that inner barrel is located above bucket is provided with taper guide plate, the taper
Guide plate is connected with central tube bottom, and cylinder body bottom position corresponding with water inlet pipe is provided with taper reflecting plate, the bucket bottom
It is communicated with the outside by discharge pipeline, return duct and sludge out pipe, return duct and water inlet pipe phase is connected on the discharge pipeline
Connection, is mounted on electric butterfly valve on the discharge pipeline, return duct, sludge out pipe and water inlet pipe, mud extraction tube end is provided with mud discharging mouth,
The cylinder lateral wall is provided with evacuation port, and cylinder lateral wall is from top to bottom sequentially provided with charging aperture, discharge port.
Preferably, stripping tube is provided with the cylinder, the stripping tube is communicated with the outside by gas-liquid separator.
Preferably, the air inlet pipe is provided with aeration plate.
Preferably, guide shell is provided between the bucket and petal type eddy flow cloth bucket, the upper and lower surface of guide shell is all provided with
There is opening.
Preferably, the position in the cylinder above stripping tube is provided with ceramics filling, and cylinder is provided with effluent weir, institute
State and be provided with inside inner cylinder biological mud, floating stuffing is provided with the oxygen consumption area.
The advantage of the invention is that：This kind of vertical microkinetic self-loopa efficient sewage treatment installation：
1st, upright type of design, determinants area is few, and space availability ratio is high；
2nd, each area does not need additional disturbance (or stirring) device, and the fluid dynamic of anaerobic zone can be partly delivered to oxygen consumption
Area, reducing energy consumption.
Brief description of the drawings
Fig. 1 is a kind of structural representation of vertical microkinetic self-loopa efficient sewage treatment installation of the present invention.
Fig. 2 is left view of the invention.
Fig. 3 right view of the invention.
Wherein：1- base plates, 2- cylinders, 3- water inlet pipes, 4- inner cylinders, 5- eddy flow water distributors, 6- air inlets, 7- air inlet pipe, 8-
Petal type eddy flow cloth bucket, 9- aeration plates, 10- discharge ports, 11- guide shells, 12- charging apertures, 13- bafflers, 14- buckets, 15-
Taper guide plate, 16- stripping tubes, 17- ceramics fillings, 18- effluent weirs, 19- central tubes, 20- delivery ports, 21- discharge pipelines, 22- electricity
Dynamic butterfly valve, 23- mud discharging mouths, 24- sewage inlet ports, 25- evacuation ports, 26- taper reflecting plates, 27- return ducts, 28- sludge out pipe,
29- floating stuffings, 30- oxygen consumptions area, 31- gas-liquid separators, 32- anoxic zones, 33- anaerobic zones.
Specific embodiment
For technological means, creation characteristic, reached purpose and effect for making present invention realization are easy to understand, with reference to
Specific embodiment, is expanded on further the present invention.
For technological means, creation characteristic, reached purpose and effect for making present invention realization are easy to understand, with reference to
Specific embodiment, is expanded on further the present invention.
As shown in Figure 1-Figure 3, a kind of vertical microkinetic self-loopa efficient sewage treatment installation, including processing equipment body,
The processing equipment body includes being provided with anaerobic zone 33, oxygen consumption in base plate 1 and the cylinder 2 on base plate 1, the cylinder 2
Area 30 and anoxic zone 32, the anoxic zone 32 include being provided with water inlet pipe 3 in inner cylinder 4, the inner cylinder 4, and the water inlet pipe 3 passes through cylinder
Body 2 is communicated with the outside, and the end of water inlet pipe 3 is provided with sewage inlet port 24, and the oxygen consumption area 30 includes petal type eddy flow cloth bucket
8th, bucket 14 and baffler 13, cylinder 2, petal type eddy flow cloth bucket 8, bucket 14 and baffler 13 surround oxygen consumption area 30, this area
Sullage rotational flow rises in domain, and water (flow) direction is identical with anaerobic zone 33, and the petal type eddy flow cloth bucket 8 is located at the top of inner cylinder 4, flower
The lower edge of flap-type eddy flow cloth bucket 8 and the welded top of inner cylinder 4, the bucket 14 are connected with baffler 13, and baffler 13 is in resistance
Make oxygen consumption area 30 while floating stuffing 29 in the absence of dead angle, be provided with air inlet pipe 7 in petal type eddy flow cloth bucket 8, it is described enter
One end of tracheae 7 is communicated with the outside, and the end of air inlet pipe 7 is provided with air inlet 6, and the anaerobic zone 33 is located at cylinder 2 and inner cylinder 4
Between, cylinder 2, inner cylinder 4 surround anaerobic zone 33 with petal type eddy flow cloth bucket 8, and from top to bottom annular rises current, finally by flower
The opening of flap-type eddy flow cloth bucket 8 enters oxygen consumption area 30, and the opening direction of petal type eddy flow cloth bucket 8 goes out with eddy flow water distributor 5
Water direction is identical, is provided with eddy flow water distributor 5 outside inner cylinder 4, after sewage enters inner cylinder 4 from water inlet pipe 3, from inner cylinder 4 close to top
Into eddy flow water distributor 5, the top of the cylinder 2 is provided with central tube 19, and small portion of gas rises along central tube 19 and discharges cylinder
2, the position that cylinder 2 is internally located at the top of bucket 14 is provided with taper guide plate 15, the taper guide plate 15 and the bottom phase of central tube 19
Connection, sewage is flowed up from after the discharge of taper guide plate 15, and mud flows downward into bucket 14, the bottom of cylinder 2 and water inlet pipe 3
Corresponding position is provided with taper reflecting plate 26, and for by the diverging of the side of current direction four, making mud float, such as the discharge of sewage is big,
Taper reflecting plate 26 can be removed, and the delivery port 20 of water inlet pipe 3 is changed to annular discharge structure, the bottom of the bucket 14 is by row
Mud pipe 21 is communicated with the outside, and return duct 27 and sludge out pipe 28, return duct 27 and water inlet are connected on the discharge pipeline 21
Pipe 3 is connected, and inner cylinder 4, the mud of cylinder 2 can also be discharged reversely from water inlet pipe 3, the discharge pipeline 21, return duct 27, mud extraction
Electric butterfly valve 22 is mounted on pipe 28 and water inlet pipe 3, makes control more flexible, the end of sludge out pipe 28 is provided with mud discharging mouth 23, institute
State the side wall of cylinder 2 and be provided with evacuation port 25, can empty in cylinder 2 such as mud, sewage lamp material, the side wall of cylinder 2 is from top to bottom successively
It is provided with charging aperture 12, discharge port 10.
It is worth noting that, being provided with stripping tube 16 in the cylinder 2, most of gas rises along this and discharges cylinder 2, pipe
In addition to because increasing the power that sewage possesses, the power for also being brought with stripping, the stripping tube 16 passes through gas to interior flow of fluid
Liquid/gas separator 31 is communicated with the outside, and the air inlet pipe 7 is provided with aeration plate 9, to the oxygen supply of oxygen consumption area 30.
In the present embodiment, guide shell 11, the guide shell 11 are provided between the bucket 14 and petal type eddy flow cloth bucket 8
Upper and lower surface is equipped with opening, and the air of aeration plate 9 is located at vapour by being reached after guide shell 11 in baffler 13, the cylinder 2
The position for carrying the top of pipe 16 is provided with ceramics filling 17, and for intercepting suspension, such as mud, cylinder 2 is provided with effluent weir 18, institute
State and biological mud is provided with inside inner cylinder 4, floating stuffing 29 is provided with the oxygen consumption area 30.
Based on above-mentioned, this kind of vertical microkinetic self-loopa efficient sewage treatment installation, upright type of design, determinants area
Few, space availability ratio is high, and each area does not need additional disturbance (or stirring) device, and the fluid dynamic of anaerobic zone 33 can partly to pass
It is handed to oxygen consumption area 30, reducing energy consumption, the invention provides a kind of low, space availability ratio vertical fine motion high, rational in infrastructure of consuming energy
Power self-loopa efficient sewage treatment installation.
As known by the technical knowledge, the present invention can be by other essence without departing from its spirit or the embodiment party of essential feature
Case is realized.Therefore, embodiment disclosed above, for each side, is all merely illustrative, and is not only.Institute
Have within the scope of the present invention or be included in the invention in the change being equal in the scope of the present invention.
Claims (5)
1. a kind of vertical microkinetic self-loopa efficient sewage treatment installation, including processing equipment body, it is characterised in that the place
Reason apparatus body includes base plate and the cylinder on base plate, and anaerobic zone, oxygen consumption area and anoxic zone, institute are provided with the cylinder
Stating anoxic zone includes inner cylinder, and water inlet pipe is provided with the inner cylinder, and the water inlet pipe is communicated with the outside through cylinder, pipe end of intaking
Portion is provided with sewage inlet port, and the oxygen consumption area includes petal type eddy flow cloth bucket, bucket and baffler, the petal type eddy flow cloth
Bucket is connected located at inner cylinder top, the bucket with baffler, and air inlet pipe, the air inlet are provided with petal type eddy flow cloth bucket
One end of pipe is communicated with the outside, and air inlet tube end is provided with air inlet, and the anaerobic zone is located between cylinder and inner cylinder, outside inner cylinder
Eddy flow water distributor is provided with, the cylinder top is provided with central tube, and the position that inner barrel is located above bucket is provided with taper guide plate,
The taper guide plate is connected with central tube bottom, and cylinder body bottom position corresponding with water inlet pipe is provided with taper reflecting plate, described
Bucket bottom is communicated with the outside by discharge pipeline, is connected to return duct and sludge out pipe on the discharge pipeline, return duct with
Water inlet pipe is connected, and electric butterfly valve is mounted on the discharge pipeline, return duct, sludge out pipe and water inlet pipe, and mud extraction tube end sets
There is mud discharging mouth, the cylinder lateral wall is provided with evacuation port, and cylinder lateral wall is from top to bottom sequentially provided with charging aperture, discharge port.
2. a kind of vertical microkinetic self-loopa efficient sewage treatment installation according to claim 1, it is characterised in that：It is described
Stripping tube is provided with cylinder, the stripping tube is communicated with the outside by gas-liquid separator.
3. a kind of vertical microkinetic self-loopa efficient sewage treatment installation according to claim 1, it is characterised in that：It is described
Air inlet pipe is provided with aeration plate.
4. a kind of vertical microkinetic self-loopa efficient sewage treatment installation according to claim 3, it is characterised in that：It is described
Guide shell is provided between bucket and petal type eddy flow cloth bucket, the upper and lower surface of guide shell is equipped with opening.
5. a kind of vertical microkinetic self-loopa efficient sewage treatment installation according to claim 1, it is characterised in that：It is described
Position in cylinder above stripping tube is provided with ceramics filling, and cylinder is provided with effluent weir, biology is provided with inside the inner cylinder
Mud, floating stuffing is provided with the oxygen consumption area.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710128890.8A CN106865765B (en) | 2017-03-06 | 2017-03-06 | Vertical micro-power self-circulation efficient sewage treatment equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710128890.8A CN106865765B (en) | 2017-03-06 | 2017-03-06 | Vertical micro-power self-circulation efficient sewage treatment equipment |
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| Publication Number | Publication Date |
|---|---|
| CN106865765A true CN106865765A (en) | 2017-06-20 |
| CN106865765B CN106865765B (en) | 2023-05-26 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710128890.8A Active CN106865765B (en) | 2017-03-06 | 2017-03-06 | Vertical micro-power self-circulation efficient sewage treatment equipment |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109928501A (en) * | 2019-04-09 | 2019-06-25 | 东华大学 | A kind of high-performance bio fluidized-bed reactor |
Citations (7)
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| JPH09323092A (en) * | 1996-06-04 | 1997-12-16 | Hokoku Kogyo Co Ltd | Sewage treating device |
| WO1999064359A1 (en) * | 1998-06-09 | 1999-12-16 | Noyes-Tipton, L.L.C. | Wastewater treatment system |
| CA2481853A1 (en) * | 2004-10-12 | 2006-04-12 | Laleh Yerushalmi | Integrated multi-zone wastewater treatment system and method |
| CN101768887A (en) * | 2010-03-17 | 2010-07-07 | 山东泉林纸业有限责任公司 | Circular utilization method of straw in pulping and papermaking processes |
| CN105399277A (en) * | 2015-12-12 | 2016-03-16 | 常州大学 | Rural sewage treatment apparatus |
| CN106242050A (en) * | 2016-07-27 | 2016-12-21 | 广州鹏凯环境科技股份有限公司 | Circular integration sewage disposal device in a kind of vertical low energy consumption |
| CN206570089U (en) * | 2017-03-06 | 2017-10-20 | 肇庆市鹏凯环保装备有限公司 | A kind of vertical microkinetic self-loopa efficient sewage treatment installation |
-
2017
- 2017-03-06 CN CN201710128890.8A patent/CN106865765B/en active Active
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH09323092A (en) * | 1996-06-04 | 1997-12-16 | Hokoku Kogyo Co Ltd | Sewage treating device |
| WO1999064359A1 (en) * | 1998-06-09 | 1999-12-16 | Noyes-Tipton, L.L.C. | Wastewater treatment system |
| CA2481853A1 (en) * | 2004-10-12 | 2006-04-12 | Laleh Yerushalmi | Integrated multi-zone wastewater treatment system and method |
| CN101768887A (en) * | 2010-03-17 | 2010-07-07 | 山东泉林纸业有限责任公司 | Circular utilization method of straw in pulping and papermaking processes |
| CN105399277A (en) * | 2015-12-12 | 2016-03-16 | 常州大学 | Rural sewage treatment apparatus |
| CN106242050A (en) * | 2016-07-27 | 2016-12-21 | 广州鹏凯环境科技股份有限公司 | Circular integration sewage disposal device in a kind of vertical low energy consumption |
| CN206570089U (en) * | 2017-03-06 | 2017-10-20 | 肇庆市鹏凯环保装备有限公司 | A kind of vertical microkinetic self-loopa efficient sewage treatment installation |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109928501A (en) * | 2019-04-09 | 2019-06-25 | 东华大学 | A kind of high-performance bio fluidized-bed reactor |
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| CN106865765B (en) | 2023-05-26 |
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Address after: 526238 No. 2, Gangnan street, high tech Industrial Development Zone, Zhaoqing City, Guangdong Province Patentee after: Guangdong Pengkai Intelligent Equipment Manufacturing Co.,Ltd. Address before: 526238 No. 2, Wende Third Street, high tech Zone, Zhaoqing City, Guangdong Province Patentee before: ZHAOQING PENGKAI ENVIRONMENTAL PROTECTION EQUIPMENT Co.,Ltd. |