CN206570089U - 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
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- CN206570089U CN206570089U CN201720209983.9U CN201720209983U CN206570089U CN 206570089 U CN206570089 U CN 206570089U CN 201720209983 U CN201720209983 U CN 201720209983U CN 206570089 U CN206570089 U CN 206570089U
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Abstract
The utility model 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 bottom plate and the cylinder on bottom 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, tube end of intaking 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 that the utility model provides a kind of power consumption, space availability ratio is high, vertical microkinetic self-loopa efficient sewage treatment installation rational in infrastructure.
Description
Technical field
The utility model is related to technical field of sewage treatment equipment, and in particular to a kind of vertical microkinetic self-loopa high-efficient sewage
Water treatment facilities.
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
It is only possible to complete whole sewage disposal process by two or more method, its equipment is based on building construction, machine
Based on unit cell supplemented by electric equipment, floor space is there is greatly, investment is high, operating cost is high, anti-load-bearing capacity is poor, reaction
Efficiency is low, manage compared with falling behind, the problem of device efficiency is low.A similar work is continued to use in the processing to sewage always at present
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 equipment of A2/0 or inversion A 2/0, its anaerobic zone, anoxic zone, oxygen consumption area are that formula arrangement of lying (is appreciated that
For 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, designs a kind of efficient sewage treatment installation that can solve the problem that problem above
Become urgent problem to be solved.
Utility model content
The purpose of this utility model is to provide a kind of vertical microkinetic self-loopa efficient sewage treatment installation, existing to solve
Above-mentioned multinomial defect caused by having in technology.
A kind of vertical microkinetic self-loopa efficient sewage treatment installation, including processing equipment body, the processing equipment sheet
Body includes being provided with anaerobic zone, oxygen consumption area and anoxic zone, the anoxic zone in bottom plate and the cylinder on bottom plate, 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
Above inner cylinder, 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
Central tube is provided with the top of water distributor, the cylinder, 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
Electric butterfly valve is mounted on connection, 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.
It is preferred that, stripping tube is provided with the cylinder, the stripping tube is communicated with the outside by gas-liquid separator.
It is preferred that, the air inlet pipe is provided with aeration plate.
It is preferred that, guide shell is provided between bucket and petal type eddy flow the cloth bucket, the upper and lower surface of guide shell is all provided with
There is opening.
It is preferred that, the position in the cylinder above stripping tube is provided with ceramics filling, and cylinder is provided with effluent weir, institute
State to be provided with inside inner cylinder in biological mud, the oxygen consumption area and be provided with floating stuffing.
The utility model has the advantage of：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, reduces energy consumption.
Brief description of the drawings
Fig. 1 is a kind of structural representation of vertical microkinetic self-loopa efficient sewage treatment installation described in the utility model
Figure.
Fig. 2 is left view of the present utility model.
Fig. 3 right views of the present utility model.
Wherein：1- bottom 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.
Embodiment
To be easy to understand technological means, creation characteristic, reached purpose and effect of the utility model realization, below
With reference to embodiment, the utility model is expanded on further.
To be easy to understand technological means, creation characteristic, reached purpose and effect of the utility model realization, below
With reference to embodiment, the utility model is expanded on further.
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 bottom plate 1 and the cylinder 2 on bottom 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 is welded with the top of inner cylinder 4, and the bucket 14 is connected with baffler 13, and baffler 13 is in resistance
Make oxygen consumption area 30 that dead angle is not present while floating stuffing 29, 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, and the outside of inner cylinder 4 is provided with eddy flow water distributor 5, and sewage enters after inner cylinder 4 from water inlet pipe 3, from inner cylinder 4 close to top
Into eddy flow water distributor 5, the top of 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 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, for the side of current direction four to be dissipated, mud is floated, 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 bucket 14 passes through 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
The side wall of cylinder 2 is stated provided with evacuation port 25, can be emptied in cylinder 2 such as mud, sewage lamp material, the side wall of cylinder 2 is from top to bottom successively
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, manages
Interior flow of fluid is in addition to the power possessed by increase sewage, and the power also brought with stripping, the stripping tube 16 passes through gas
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 bucket 14 and petal type eddy flow the cloth bucket 8
Upper and lower surface is equipped with opening, and the air of aeration plate 9 is reached after guide shell 11 is located at vapour in baffler 13, the cylinder 2
The position for carrying the top of pipe 16 is provided with ceramics filling 17, and for obstructing suspension, such as mud, cylinder 2 is provided with effluent weir 18, institute
The inside of inner cylinder 4 is stated provided with biological mud, the oxygen consumption area 30 is interior to be provided with floating stuffing 29.
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 be passed partly
It is handed to oxygen consumption area 30, reduces energy consumption, the utility model provides a kind of high, rational in infrastructure vertical of low, space availability ratio that consumes energy
Microkinetic self-loopa efficient sewage treatment installation.
As known by the technical knowledge, the utility model can be by the realities of other essence or essential feature without departing from its spirit
Scheme is applied to realize.Therefore, embodiment disclosed above, for each side, is all merely illustrative, and is not only
's.All changes in the range of the utility model or in the range of the utility model is equal to are by the utility model bag
Contain.
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
Managing apparatus body includes being provided with anaerobic zone, oxygen consumption area and anoxic zone, institute in bottom plate and the cylinder on bottom plate, the cylinder
Stating anoxic zone includes being provided with water inlet pipe in inner cylinder, 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 above inner cylinder, and the bucket is connected 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
Provided with eddy flow water distributor, central tube is provided with the top of the cylinder, 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 is set
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 inside effluent weir, the inner cylinder provided with biology
Floating stuffing is provided with mud, the oxygen consumption area.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720209983.9U CN206570089U (en) | 2017-03-06 | 2017-03-06 | A kind of vertical microkinetic self-loopa efficient sewage treatment installation |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720209983.9U CN206570089U (en) | 2017-03-06 | 2017-03-06 | A kind of vertical microkinetic self-loopa efficient sewage treatment installation |
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| Publication Number | Publication Date |
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| CN206570089U true CN206570089U (en) | 2017-10-20 |
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| CN201720209983.9U Active CN206570089U (en) | 2017-03-06 | 2017-03-06 | A kind of vertical microkinetic self-loopa efficient sewage treatment installation |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106865765A (en) * | 2017-03-06 | 2017-06-20 | 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 CN201720209983.9U patent/CN206570089U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106865765A (en) * | 2017-03-06 | 2017-06-20 | 肇庆市鹏凯环保装备有限公司 | A kind of vertical microkinetic self-loopa efficient sewage treatment installation |
| CN106865765B (en) * | 2017-03-06 | 2023-05-26 | 肇庆市鹏凯环保装备有限公司 | Vertical micro-power self-circulation efficient sewage treatment equipment |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CP03 | Change of name, title or address |
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. |
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| CP03 | Change of name, title or address |