CN208532315U - Eddy flow oxygenator - Google Patents
Eddy flow oxygenator Download PDFInfo
- Publication number
- CN208532315U CN208532315U CN201821072768.XU CN201821072768U CN208532315U CN 208532315 U CN208532315 U CN 208532315U CN 201821072768 U CN201821072768 U CN 201821072768U CN 208532315 U CN208532315 U CN 208532315U
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- eddy flow
- cylinder
- air inlet
- equipment
- oxygenator
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Abstract
The utility model discloses a kind of eddy flow oxygenator, including cylinder and air inlet injector, the lower part of the cylinder connects the taper bucket, and the cylinder top connects end socket.The eddy flow oxygenator, the combination of air inlet injector and eddy flow oxygenator apparatus body is ideally utilized, sewage is pre-processed, while removing raw water sand grains, pre-exposure gas disposal has been carried out to raw water, organic matter in degradation sewage, be conducive to subsequent biochemical treatment, the eddy flow oxygenator is used to substitute the setting pot of the prior art, compared with the setting pot of any form before, its treatment effeciency and treatment effect are well very much, and the device is steel systeming equipment, it is simple and compact for structure, it is applied widely, it is not required to separately set sediment outflow equipment, greatly reduce equipment investment and occupation area of equipment, equipment operation is easy to operate, it is easy to maintain, other than raw water intake pump, it is not required to other power sources, it saves energy consumption, operating cost is low.
Description
Technical field
The utility model belongs to municipal wastewater pre-processing device technical field, and in particular to a kind of eddy flow oxygenator.
Background technique
With China's expanding economy, the demand of one side China water resource is being sharply increased, another aspect China water
Pollution condition is still very serious, and municipal wastewater handles total amount and is continuously improved, with the general trend of new countryside construction, to life in the countryside
The process demand of sewage is increasing, and cities and towns, the black smelly problem in rural area river are still generally existing, it would be highly desirable to solve.
These sewage treatment conventional process usually will first pre-process sewage, typical primary treatment processes and second level
The pretreatment for the treatment of process generallys use raw water and removes the susceptible to plugging sundries such as pipeline water pump through grid, then pump promoted raw water into
Enter setting pot, then through sedimentation basin/primary sedimentation pond, subsequent biochemical etc. is gone to handle.The effect of setting pot mainly removes in decontaminated water
Inorganic particulate matter, protective conduit and pump mitigate the load of sedimentation basin from wearing and block, by inorganic particle and organic matter point
It does not separate, improves the containing ratio and utility value of sludge organic components.
The type of setting pot is more, but exists mostly and such as take up a large area, and structures are complicated, and cost is high, and treatment effeciency is low,
Sediment outflow is more difficult or mechanical equipment is complicated, and maintenance capacity increase leads to fluctuation of service.Currently, sewage treatment is used more
Setting pot has rotational flow grit chamber and aerated grit chamber.Rotational flow grit chamber is to be vortexed to separate sand grains with organic matter using waterpower, is arranged
Sand mode is bottom sand pump sediment outflow or airlift sediment outflow;Aerated grit chamber is to transport pool inner water stream helically
It is dynamic, it generates centrifugal force and throws out the inorganic particulate matters such as sand grains and separation of sinking, sediment outflow mode sand pump or mechanical sediment outflow.
Rotational flow grit chamber and the comparison of aerated grit chamber disadvantage are as follows.
Rotational flow grit chamber needs to grasp water flow when in use, should be in good condition, otherwise treatment effeciency declines;Aerated grit chamber
To master aeration intensity when in use, otherwise treatment effeciency declines, and energy consumption is high, and operating cost is high.
Utility model content
The purpose of this utility model is to provide a kind of eddy flow oxygenators, to solve mentioned above in the background art ask
Topic.
To achieve the above object, the utility model provides the following technical solutions: a kind of eddy flow oxygenator, including cylinder and into
Gas blowout emitter, the lower part of the cylinder connect the taper bucket, and the cylinder top connects end socket, the jet port of the air inlet injector
The eddy flow water inlet pipe tangentially connected with eddy flow oxygenator cylinder is connected, and the air inlet injector is equipped with original water inlet and air
Import, the top position of the barrel upper seal head are equipped with water outlet, and the taper bucket bottom is equipped with sand export.
Preferably, the cylinder internal pressure control is in 0.15-0.25MPa, and air inlet injector outlet pressure is not less than
0.3Mpa。
The technical effect and advantage of the utility model: air inlet injector and eddy flow is ideally utilized in the eddy flow oxygenator
The combination of oxygenator apparatus body, pre-processes sewage, while removing raw water sand grains, has carried out pre-exposure to raw water
Gas disposal, the organic matter in sewage of degrading, is conducive to subsequent biochemical treatment, the eddy flow oxygenator is for substituting the prior art
Setting pot, the setting pot in the form of any one before compare, and treatment effeciency and treatment effect are well very much, and should
Device is steel systeming equipment, simple and compact for structure, applied widely, is not required to separately set sediment outflow equipment, greatly reduce equipment investment with
Occupation area of equipment, equipment operation is easy to operate, easy to maintain, other than raw water intake pump, is not required to other power sources, saves
Energy consumption, operating cost are low.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the utility model;
Fig. 2 is the structure top view of A-A at the utility model Fig. 1.
In figure: 1 cylinder, 2 the taper buckets, 3 end sockets, 4 air inlet injectors, 5 former water inlets, 6 air intlets, 7 eddy flow water inlet pipes,
8 water outlets, 9 sand exports.
Specific embodiment
The following will be combined with the drawings in the embodiments of the present invention, carries out the technical scheme in the embodiment of the utility model
Clearly and completely describe, it is clear that the described embodiments are only a part of the embodiments of the utility model, rather than whole
Embodiment.Based on the embodiments of the present invention, those of ordinary skill in the art are without making creative work
Every other embodiment obtained, fall within the protection scope of the utility model.
The utility model provides a kind of eddy flow oxygenator as shown in Figs. 1-2, including cylinder 1 and air inlet injector 4, institute
The lower part connection the taper bucket 2 of cylinder 1 is stated, 1 top of cylinder connects end socket 3, the jet port and eddy flow of the air inlet injector 4
The tangentially connected eddy flow water inlet pipe 7 of oxygenator cylinder 1 is connected, the air inlet injector 4 be equipped with original water inlet 5 and air into
Mouth 6, the top position of 1 upper cover 3 of cylinder are equipped with water outlet 8, and 2 bottom of the taper bucket is equipped with sand export 9.
Specifically, pressure is controlled in 0.15-0.25MPa in the cylinder 1, and 4 outlet pressure of air inlet injector is not less than
0.3Mpa, to ensure the efficient process of eddy flow oxygenation.
The eddy flow oxygenator, in the case of sewage generates certain pressure through impeller of pump high speed rotation when in use, sewage is with height
Speed enters air inlet injector 4 from original water inlet 5, sprays from 4 nozzle of air inlet injector, and swiftly flowing sewage passes through mixing chamber
When, vacuum is formed in mixing chamber, large quantity of air is sucked by air intlet 6, after air enters mixing chamber, in 4 larynx of air inlet injector
It is vigorously mixed at pipe with sewage, air is cut into micro air bubble by sewage, and air quickly dissolves in water under a certain pressure, in gas
Water generates sharp impacts and simultaneously separates the organic matter for being attached to surface particles in sewage with friction, forms gas, liquid, solid mixing
Object is discharged into 7 tangential swirl of eddy flow water inlet pipe by diffuser and enters inside cylinder 1.And the sewage containing air-liquid, solid mixture is revolving
Under the action of the centrifugal force, centripetal force and the Fluid pressure that generate in stream motion process, solid particulate matter is deposited to equipment cone quickly
Bottom is expelled directly out by bottom sand export 9, and the rapid increase under cyclonic action of the dissolved oxygen organic matter sewage with micro air bubble,
It is discharged from eddy flow oxygenator equipment top delivery port 8.
Finally, it should be noted that the above descriptions are merely preferred embodiments of the present invention, it is not limited to this
Utility model, although the utility model is described in detail with reference to the foregoing embodiments, for those skilled in the art
For, it is still possible to modify the technical solutions described in the foregoing embodiments, or to part of technical characteristic
It is equivalently replaced, within the spirit and principle of the utility model, any modification, equivalent replacement, improvement and so on,
It should be included within the scope of protection of this utility model.
Claims (2)
1. a kind of eddy flow oxygenator, including cylinder (1) and air inlet injector (4), it is characterised in that: the lower part of the cylinder (1)
It connects the taper bucket (2), cylinder (1) top connects end socket (3), and the jet port and eddy flow of the air inlet injector (4) are oxygenated
The tangentially connected eddy flow water inlet pipe (7) of device cylinder (1) is connected, and the air inlet injector (4) is equipped with original water inlet (5) and empty
The top position of gas import (6), cylinder (1) upper cover (3) is equipped with water outlet (8), and the taper bucket (2) bottom is equipped with
Sand mouth (9).
2. a kind of eddy flow oxygenator according to claim 1, it is characterised in that: the interior pressure control of cylinder (1) exists
0.15-0.25MPa, and air inlet injector (4) outlet pressure is not less than 0.3Mpa.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201821072768.XU CN208532315U (en) | 2018-07-09 | 2018-07-09 | Eddy flow oxygenator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201821072768.XU CN208532315U (en) | 2018-07-09 | 2018-07-09 | Eddy flow oxygenator |
Publications (1)
Publication Number | Publication Date |
---|---|
CN208532315U true CN208532315U (en) | 2019-02-22 |
Family
ID=65388176
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201821072768.XU Active CN208532315U (en) | 2018-07-09 | 2018-07-09 | Eddy flow oxygenator |
Country Status (1)
Country | Link |
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CN (1) | CN208532315U (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
RU200367U1 (en) * | 2020-03-11 | 2020-10-21 | Федеральное государственное бюджетное образовательное учреждение высшего образования "Петрозаводский государственный университет" | OXYGENATOR |
CN115845423A (en) * | 2022-11-17 | 2023-03-28 | 华东理工大学 | Device and method for strengthening gas-liquid mass transfer by utilizing local circulation and bubble cyclone |
-
2018
- 2018-07-09 CN CN201821072768.XU patent/CN208532315U/en active Active
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
RU200367U1 (en) * | 2020-03-11 | 2020-10-21 | Федеральное государственное бюджетное образовательное учреждение высшего образования "Петрозаводский государственный университет" | OXYGENATOR |
CN115845423A (en) * | 2022-11-17 | 2023-03-28 | 华东理工大学 | Device and method for strengthening gas-liquid mass transfer by utilizing local circulation and bubble cyclone |
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