CN206872510U - A kind of spiral aerobic biofilm reactor - Google Patents
A kind of spiral aerobic biofilm reactor Download PDFInfo
- Publication number
- CN206872510U CN206872510U CN201720600401.XU CN201720600401U CN206872510U CN 206872510 U CN206872510 U CN 206872510U CN 201720600401 U CN201720600401 U CN 201720600401U CN 206872510 U CN206872510 U CN 206872510U
- Authority
- CN
- China
- Prior art keywords
- reative cell
- appendix
- flow regulator
- biofilm reactor
- helical form
- 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
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Classifications
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- 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
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- Apparatus Associated With Microorganisms And Enzymes (AREA)
Abstract
The utility model discloses a kind of spiral aerobic biofilm reactor, belong to film reaction apparatus field, including reative cell and flow regulator, the reative cell is arranged on above frame platform, filling tube and aeration tube are installed on the shell of the reative cell, end cap is provided with above the reative cell, the reative cell is connected by the flow regulator with discharge nozzle, the reative cell is by helical form biomembrane, appendix and gas escape window composition, the gas escape window is arranged at the center of the reative cell, and connected with the appendix, the helical form biomembrane is provided with the side wall of the appendix.Beneficial effect is：The utility model expands reaction contact area while smaller land area is taken, so as to improve reaction efficiency, have aeration quantity it is small, energy-conservation effect, while can the row's of control material speed.
Description
Technical field
The utility model belongs to film reaction apparatus field, and in particular to a kind of spiral aerobic biofilm reactor.
Background technology
The new technology that membrane reactor is membrane process and course of reaction is combined, the step of being provided simultaneously with reacting and separated.
In the last few years, as the development of biotechnology, the various equipment that sewage disposal is carried out by aerobe constantly update the replacement, are
Sewage disposal is made that contribution.There is reaction contact area is small, reaction speed for aerobic biofilm reactor in the market
Slowly the shortcomings that, corresponding speed is slow.
Utility model content
The purpose of this utility model is that to solve the above problems and provides a kind of spiral aerobic biofilm reactor.
The utility model is achieved through the following technical solutions above-mentioned purpose：
A kind of spiral aerobic biofilm reactor, including reative cell and flow regulator, the reative cell are arranged on frame
Above platform, filling tube and aeration tube are installed on the shell of the reative cell, end cap is provided with above the reative cell, it is described anti-
Room is answered to be connected by the flow regulator with discharge nozzle, the reative cell is escaped by helical form biomembrane, appendix and gas
Escaped window composition, and the gas escape window is arranged at the center of the reative cell, and is connected with the appendix, the appendix
Side wall on be provided with the helical form biomembrane.
In said structure, the material of pending oxidation processes is injected in the reative cell by the filling tube, led to simultaneously
Cross the aeration tube and inject air into the appendix, in the presence of the helical form biomembrane, in the appendix
Air carries out oxidation reaction by the material in the helical form biomembrane and the reative cell, and the air after reacting is by described
Gas escape window escapes out, and spills into air, and reacted material is under the control of the flow regulator by the discharging
Pipe emits.
In order to further improve performance of the present utility model, the frame platform is fixed with the reative cell by rivet
Connection, the reative cell are connected with the filling tube by pipe collar, and the appendix is connected with the aeration tube by pipe collar.
In order to further improve performance of the present utility model, the helical form biomembrane is pasted with the appendix
Together, the appendix is fixedly connected with the gas escape window.
In order to further improve performance of the present utility model, the reative cell passes through valve with the flow regulator
Connection, the flow regulator are fixedly connected with the discharge nozzle.
In order to further improve performance of the present utility model, the end cap is connected with the reative cell by hinge.
Beneficial effect is：The utility model expands reaction contact area while smaller land area is taken, so as to
Improve reaction efficiency, have aeration quantity it is small, energy-conservation effect, while can the row's of control material speed.
Brief description of the drawings
Fig. 1 is a kind of front view of spiral aerobic biofilm reactor described in the utility model；
Fig. 2 is a kind of top view of the reative cell of spiral aerobic biofilm reactor described in the utility model.
Description of reference numerals is as follows：
1st, frame platform；2nd, filling tube；3rd, reative cell；4th, end cap；5th, aeration tube；6th, flow regulator；7th, discharge nozzle；
301st, helical form biomembrane；302nd, appendix；303rd, gas escape window.
Embodiment
The utility model is described in further detail below in conjunction with the accompanying drawings：
As Figure 1-Figure 2, a kind of spiral aerobic biofilm reactor, including reative cell 3 and flow regulator 6, reaction
Room 3 is arranged on the top of frame platform 1, and filling tube 2 and aeration tube 5 are provided with the shell of reative cell 3, and the top of reative cell 3 is provided with
End cap 4, reative cell 3 are connected by flow regulator 6 with discharge nozzle 7, and reative cell 3 is by helical form biomembrane 301, appendix
302 and gas escape window 303 form, gas escape window 303 is arranged at the center of reative cell 3, and is connected with appendix 302,
Helical form biomembrane 301 is provided with the side wall of appendix 302.
In said structure, the material of pending oxidation processes is injected in reative cell 3 by filling tube 2, while pass through aeration
Pipe 5 injects air into appendix 302, and in the presence of helical form biomembrane 301, the air in appendix 302 passes through spiral
Shape biomembrane 301 carries out oxidation reaction with the material in reative cell 3, and the air after reacting is escaped out by gas escape window 303
Go, spill into air, reacted material is emitted under the control of flow regulator 6 by discharge nozzle 7.
In order to further improve performance of the present utility model, frame platform 1 is fixedly connected with reative cell 3 by rivet,
Frame platform 1 can be that reative cell 3 provides structural support, and reative cell 3 is connected with filling tube 2 by pipe collar, can pass through filling tube 2
By in pending material injection reative cell 3, in case reacting, appendix 302 is connected by pipe collar with aeration tube 5, can passed through
Aeration tube 5 injects reaction in appendix 302 with air, together with helical form biomembrane 301 is pasted with appendix 302, gas transmission
Pipe 302 can be that helical form biomembrane 301 provides structural support, and helical form biomembrane 301 can be aerobe and material
Reaction provides space, and appendix 302 is fixedly connected with gas escape window 303, and reacted air can be from gas escape window 303
Distribute, reative cell 3 is connected with flow regulator 6 by valve, and flow regulator 6 is fixedly connected with discharge nozzle 7, reative cell
3 reacted materials can transfer out from discharge nozzle 7, flow regulator 6 can adjust material conveying speed, end cap 4 with
Reative cell 3 is connected by hinge, and end cap 4 can be that reative cell 3 provides protection.
General principle, principal character and advantage of the present utility model has been shown and described above.The technical staff of the industry
It should be appreciated that the utility model is not restricted to the described embodiments, the simply explanation described in above-described embodiment and specification is originally
The principle of utility model, on the premise of the spirit and scope of the utility model is not departed from, the utility model also has various change
And improvement, these changes and improvements are both fallen within claimed the scope of the utility model.The utility model requires protection scope
Defined by appended claims and its effect thing.
Claims (5)
- A kind of 1. spiral aerobic biofilm reactor, it is characterised in that：Including reative cell and flow regulator, the reative cell peace Above frame platform, filling tube and aeration tube are installed on the shell of the reative cell, end is provided with above the reative cell Lid, the reative cell are connected by the flow regulator with discharge nozzle, and the reative cell is by helical form biomembrane, appendix Formed with gas escape window, the gas escape window is arranged at the center of the reative cell, and is connected with the appendix, institute State and the helical form biomembrane is provided with the side wall of appendix.
- A kind of 2. spiral aerobic biofilm reactor according to claim 1, it is characterised in that：The frame platform with it is described Reative cell is fixedly connected by rivet, and the reative cell is connected with the filling tube by pipe collar, the appendix and the exposure Tracheae is connected by pipe collar.
- A kind of 3. spiral aerobic biofilm reactor according to claim 1, it is characterised in that：The helical form biomembrane Together with being pasted with the appendix, the appendix is fixedly connected with the gas escape window.
- A kind of 4. spiral aerobic biofilm reactor according to claim 1, it is characterised in that：The reative cell with it is described Flow regulator is connected by valve, and the flow regulator is fixedly connected with the discharge nozzle.
- A kind of 5. spiral aerobic biofilm reactor according to claim 1, it is characterised in that：The end cap with it is described anti- Room is answered to be connected by hinge.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720600401.XU CN206872510U (en) | 2017-05-26 | 2017-05-26 | A kind of spiral aerobic biofilm reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720600401.XU CN206872510U (en) | 2017-05-26 | 2017-05-26 | A kind of spiral aerobic biofilm reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206872510U true CN206872510U (en) | 2018-01-12 |
Family
ID=61337099
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720600401.XU Expired - Fee Related CN206872510U (en) | 2017-05-26 | 2017-05-26 | A kind of spiral aerobic biofilm reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206872510U (en) |
-
2017
- 2017-05-26 CN CN201720600401.XU patent/CN206872510U/en not_active Expired - Fee Related
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| 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: 20180112 Termination date: 20190526 |