CN204661420U - With the Venturi ejector of broken bubble equipment - Google Patents
With the Venturi ejector of broken bubble equipment Download PDFInfo
- Publication number
- CN204661420U CN204661420U CN201520188541.1U CN201520188541U CN204661420U CN 204661420 U CN204661420 U CN 204661420U CN 201520188541 U CN201520188541 U CN 201520188541U CN 204661420 U CN204661420 U CN 204661420U
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- CN
- China
- Prior art keywords
- mixing chamber
- cylindrical mixing
- diameter end
- jet head
- broken bubble
- 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
- 230000015572 biosynthetic process Effects 0.000 claims description 6
- 229910000831 Steel Inorganic materials 0.000 claims description 4
- 239000010959 steel Substances 0.000 claims description 4
- 239000007788 liquid Substances 0.000 abstract description 4
- 239000007789 gas Substances 0.000 description 10
- 238000005273 aeration Methods 0.000 description 6
- 230000000694 effects Effects 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 238000005276 aerator Methods 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 230000003434 inspiratory effect Effects 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 239000010802 sludge Substances 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Classifications
-
- 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
Landscapes
- Jet Pumps And Other Pumps (AREA)
Abstract
The utility model discloses a kind of Venturi ejector with broken bubble equipment, comprise the jet head docked successively, cylindrical mixing chamber and diffuser tube, described jet head is horn-like, the miner diameter end of this jet head extend in described cylindrical mixing chamber, the miner diameter end of this jet head is arranged near described cylindrical mixing chamber right-hand member, at least 2 inlet pipe are communicated with in the middle part of described cylindrical mixing chamber, this inlet pipe is tangentially arranged on described cylindrical mixing chamber, inlet pipe described in each is arranged with the central shaft centrosymmetry of cylindrical mixing chamber, the bigger diameter end of described diffuser tube is provided with the broken bubble fan of high speed rotating, this broken bubble fan is docked by the bigger diameter end of flange with described diffuser tube.A kind of Venturi ejector with broken bubble equipment of the utility model, multiple inlet pipe is tangentially ventilated, and gas distribution is even, and increase gas and liquid comes into contact area, oxygen-transfer efficiency is high.
Description
Technical field
The utility model belongs to aeration process field, specifically, relates to a kind of Venturi ejector with broken bubble equipment.
Background technology
In water treatment field, the shortcoming such as all undesirable and device structure of traditional blast aeration and the oxygen mass transfer coefficients of mechanical aeration, dissolved oxygen speed, mix and blend effect is complicated.Conventional fluidic aerator inspiratory capacity under natural aspiration mode is not enough, and to increase inspiratory capacity be generally increase water pump power and jet aerator quantity, and increase blower equipment, conventional fluidic aerator is all single Venturi ejector, and difference is the large and little of Venturi ejector, when Venturi ejector do larger time, there is gas and water engaging surface is little, can not fully by gas and liquid mixing, bubble generation is large, it is low that bubble smashes degree, affects aeration effect.
Utility model content
For solving above technical problem, the purpose of this utility model is to provide a kind of Venturi ejector with broken bubble equipment, and it is high that bubble smashes degree, and multiple inlet pipe is tangentially ventilated, and gas distribution is even, and increase gas and liquid comes into contact area, oxygen-transfer efficiency is high.
The utility model object is achieved in that a kind of Venturi ejector with broken bubble equipment, its key is: comprise the jet head docked successively, cylindrical mixing chamber and diffuser tube, described jet head is horn-like, the miner diameter end of this jet head extend in described cylindrical mixing chamber, the miner diameter end of this jet head is arranged near described cylindrical mixing chamber right-hand member, at least 2 inlet pipe are communicated with in the middle part of described cylindrical mixing chamber, this inlet pipe is tangentially arranged on described cylindrical mixing chamber, inlet pipe described in each is arranged with the central shaft centrosymmetry of cylindrical mixing chamber, the bigger diameter end of described diffuser tube is provided with the broken bubble fan of high speed rotating, this broken bubble fan is docked by the bigger diameter end of flange with described diffuser tube.
Adopt said structure, current are entered by jet head, gas enters from inlet pipe, the gas of inlet pipe enters after in cylindrical mixing chamber, mix along spiral inner wall with current, gas distribution is even, gas forms very trickle bubble under the effect of high speed strenuous exercise, simultaneously under the effect of broken bubble fan, bubble is smashed further, form more tiny bubble, add contact area, and then increase inspiratory capacity and OTR, and then increase active sludge Surface Renewal rate and adsorption surface area, thus make oxygen and useless Organic substance in water in the tiny cotton-shaped physical efficiency of active sludge and bubble have abundant Contact-sorption effect, improve aeration effect, above-mentioned broken bubble fan is detachable, and when there being broken bubble to fan, bubble is thinner, and divergence scope is wider, but jet length is near, and when jet length needs farther, then broken bubble fan can be pulled down, and improves jet length, simple to operation.
The channel diameter of above-mentioned cylindrical mixing chamber reduces to low order end gradually from inlet pipe junction, and the miner diameter end diameter of described jet head is less than described cylindrical mixing chamber right-hand member porthole diameter.
The miner diameter end diameter of above-mentioned jet head is 20-30mm, and the right-hand member porthole diameter of described cylindrical mixing chamber is 40-80mm, and the vertical range of described jet head miner diameter end and described cylindrical mixing chamber right-hand member porthole is 5-30mm.
Adopting said structure, closes up in right part in the internal passages of cylindrical mixing chamber, is compressed by air-flow, increases the severe degree of the motion of air-flow, is convenient to bubble to smash, and increases contact area.
The inwall of above-mentioned inlet pipe and diffuser tube is distributed with the rifle formation of spiral extension, this rifle formation makes air-flow or current carry out helicoidal flow when leaving pipeline.
Adopt said structure, be convenient to further bubble be smashed.
Above-mentioned diffuser tube is horn-like, and the miner diameter end of this diffuser tube docks with described cylindrical mixing chamber.
Adopt said structure, trumpet-shaped diffuser tube can increase aeration surface-area.
The bigger diameter end of above-mentioned jet head is provided with Flange joint dish, and the bigger diameter end port capping of described diffuser tube has stainless (steel) wire.
Adopt said structure, the Flange joint dish of jet head is convenient to install and is connected, and bubble can be smashed by stainless (steel) wire again.
Beneficial effect:
A kind of Venturi ejector with broken bubble equipment of the utility model, multiple inlet pipe is tangentially ventilated, and gas distribution is even, and increase gas and liquid comes into contact area, oxygen-transfer efficiency is high.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model;
Fig. 2 is the A-A sectional view of Fig. 1.
Embodiment
Below in conjunction with embodiment and accompanying drawing, the utility model is described in further detail.
Embodiment:
As illustrated in fig. 1 and 2: a kind of Venturi ejector with broken bubble equipment, by the jet head 1 docked successively, cylindrical mixing chamber 2 and diffuser tube 3 form, described jet head 1 is in horn-like, the miner diameter end of this jet head 1 extend in described cylindrical mixing chamber 2, the miner diameter end of this jet head 1 is arranged near described cylindrical mixing chamber 2 right-hand member, 2 inlet pipe 4 are communicated with in the middle part of described cylindrical mixing chamber 2, the number of certain inlet pipe also can be 3, 4, 5, 6 etc., as long as multiple inlet pipe can be realized evenly ventilate in mixing section, this inlet pipe 4 is tangentially arranged on described cylindrical mixing chamber 2, inlet pipe 4 described in each is arranged with the central shaft centrosymmetry of cylindrical mixing chamber 2, the bigger diameter end of described diffuser tube 3 is provided with the broken bubble fan 3a of high speed rotating, this broken bubble fan 3a is docked by the bigger diameter end of flange with described diffuser tube 3.
The inwall of described inlet pipe 4 and diffuser tube 3 is distributed with the rifle formation 4a of spiral extension, this rifle formation 4a makes air-flow or current carry out helicoidal flow when leaving pipeline.Described diffuser tube 3 is in horn-like, and the miner diameter end of this diffuser tube 3 docks with described cylindrical mixing chamber 2.The bigger diameter end of described jet head 1 is equipped with Flange joint dish 5, and the bigger diameter end port capping of described diffuser tube 3 has stainless (steel) wire 6.The channel diameter of described cylindrical mixing chamber 2 reduces to low order end gradually from inlet pipe 4 junction, the miner diameter end diameter of described jet head 1 is 25mm, , the right-hand member porthole diameter of described cylindrical mixing chamber 2 is 60mm, the diameter of jet head miner diameter end also can be 20, 22, 26, 30 etc., the right-hand member porthole diameter of cylindrical mixing chamber also can be 40, 50, 55, 70, 80mm etc., as long as can ensure that the diameter of jet head miner diameter end is less than the diameter of the right-hand member porthole of cylinder mixing, ensure that its size is suitable for simultaneously, the miner diameter end of described jet head 1 and the vertical range of described cylindrical mixing chamber 2 right-hand member porthole are 8.5mm, certainly this vertical range also can be 5, 6, 7, 8, 30mm etc., as long as the right-hand member of miner diameter end near cylindrical mixing chamber of jet head can be ensured, leave sufficient space to existing air-flow and current to mix, air motion degree can be improved simultaneously, smash bubble.
Claims (6)
1. the Venturi ejector with broken bubble equipment, it is characterized in that: comprise the jet head (1) docked successively, cylindrical mixing chamber (2) and diffuser tube (3), described jet head (1) is in horn-like, the miner diameter end of this jet head (1) extend in described cylindrical mixing chamber (2), the miner diameter end of this jet head (1) is arranged near described cylindrical mixing chamber (2) right-hand member, described cylindrical mixing chamber (2) middle part is communicated with at least 2 inlet pipe (4), this inlet pipe (4) is tangentially arranged on described cylindrical mixing chamber (2), inlet pipe described in each (4) is arranged with the central shaft centrosymmetry of cylindrical mixing chamber (2), the bigger diameter end of described diffuser tube (3) is provided with broken bubble fan (3a) of high speed rotating, this broken bubble fan (3a) is docked by the bigger diameter end of flange with described diffuser tube (3).
2. the Venturi ejector with broken bubble equipment according to claim 1, it is characterized in that: the channel diameter of described cylindrical mixing chamber (2) reduces to low order end gradually from inlet pipe (4) junction, the miner diameter end diameter of described jet head (1) is less than described cylindrical mixing chamber (2) right-hand member porthole diameter.
3. the Venturi ejector with broken bubble equipment according to claim 2, it is characterized in that: the miner diameter end diameter of described jet head (1) is 20-30mm, the right-hand member porthole diameter of described cylindrical mixing chamber (2) is 40-80mm, and the vertical range of described jet head (1) miner diameter end and described cylindrical mixing chamber (2) right-hand member porthole is 5-30mm.
4. the Venturi ejector with broken bubble equipment according to claim 1 or 2 or 3, it is characterized in that: the rifle formation (4a) inwall of described inlet pipe (4) and diffuser tube (3) being distributed with spiral extension, this rifle formation (4a) makes air-flow or current carry out helicoidal flow when leaving pipeline.
5. the Venturi ejector with broken bubble equipment according to claim 1 or 2 or 3, is characterized in that: described diffuser tube (3) is in horn-like, and the miner diameter end of this diffuser tube (3) docks with described cylindrical mixing chamber (2).
6. the Venturi ejector with broken bubble equipment according to claim 1 or 2 or 3, it is characterized in that: the bigger diameter end of described jet head (1) is equipped with Flange joint dish (5), the bigger diameter end port capping of described diffuser tube (3) has stainless (steel) wire (6).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520188541.1U CN204661420U (en) | 2015-03-31 | 2015-03-31 | With the Venturi ejector of broken bubble equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520188541.1U CN204661420U (en) | 2015-03-31 | 2015-03-31 | With the Venturi ejector of broken bubble equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204661420U true CN204661420U (en) | 2015-09-23 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520188541.1U Expired - Fee Related CN204661420U (en) | 2015-03-31 | 2015-03-31 | With the Venturi ejector of broken bubble equipment |
Country Status (1)
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| CN (1) | CN204661420U (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105129977A (en) * | 2015-10-10 | 2015-12-09 | 许建民 | Novel aerobiont fluidized bed reactor and technology thereof |
| CN105545235A (en) * | 2016-03-08 | 2016-05-04 | 吉林大学 | Spiral flow type foam drilling machine foam breaker |
| CN105923745A (en) * | 2016-06-28 | 2016-09-07 | 湖南农业大学 | Water body oxygenating system |
| CN106541496A (en) * | 2016-11-24 | 2017-03-29 | 陕西金石混凝土科技发展有限公司 | A kind of pneumatic aquation of dry concrete and accelerator mixed method and injection shower nozzle |
| WO2017096444A1 (en) * | 2015-12-10 | 2017-06-15 | Steiner Samar Dos Santos | Apparatus, system and method for generating nanobubbles from gases and liquid solutions |
| CN108348117A (en) * | 2015-06-30 | 2018-07-31 | 控制向导企业有限公司 | Surface treating appliance, filter and its component |
| CN109340379A (en) * | 2018-09-29 | 2019-02-15 | 同济大学 | A kind of low-temperature helium transmission sealing structure of superconducting rotating machine |
-
2015
- 2015-03-31 CN CN201520188541.1U patent/CN204661420U/en not_active Expired - Fee Related
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108348117A (en) * | 2015-06-30 | 2018-07-31 | 控制向导企业有限公司 | Surface treating appliance, filter and its component |
| CN105129977A (en) * | 2015-10-10 | 2015-12-09 | 许建民 | Novel aerobiont fluidized bed reactor and technology thereof |
| WO2017096444A1 (en) * | 2015-12-10 | 2017-06-15 | Steiner Samar Dos Santos | Apparatus, system and method for generating nanobubbles from gases and liquid solutions |
| CN105545235A (en) * | 2016-03-08 | 2016-05-04 | 吉林大学 | Spiral flow type foam drilling machine foam breaker |
| CN105923745A (en) * | 2016-06-28 | 2016-09-07 | 湖南农业大学 | Water body oxygenating system |
| CN105923745B (en) * | 2016-06-28 | 2019-01-15 | 湖南农业大学 | Water oxygenation system |
| CN106541496A (en) * | 2016-11-24 | 2017-03-29 | 陕西金石混凝土科技发展有限公司 | A kind of pneumatic aquation of dry concrete and accelerator mixed method and injection shower nozzle |
| CN109340379A (en) * | 2018-09-29 | 2019-02-15 | 同济大学 | A kind of low-temperature helium transmission sealing structure of superconducting rotating machine |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP03 | Change of name, title or address |
Address after: 400042 C1 3 floor, headquarters city, Yuzhong District, Chongqing Patentee after: CHONGQING YANGZHENG ENVIRONMENTAL PROTECTION POLYTRON TECHNOLOGIES Inc. Address before: 401147 the No. seven village of Dashi dam, Jiangbei District, Chongqing City, No. 9, 5 Patentee before: CHONGQING YZ ENVIRONMENTAL PROTECTION TECHNOLOGY Co.,Ltd. |
|
| CP03 | Change of name, title or address | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150923 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |