CN109046792A - A kind of mixed flow type microbubble generator and bubble distributer - Google Patents
A kind of mixed flow type microbubble generator and bubble distributer Download PDFInfo
- Publication number
- CN109046792A CN109046792A CN201811244061.7A CN201811244061A CN109046792A CN 109046792 A CN109046792 A CN 109046792A CN 201811244061 A CN201811244061 A CN 201811244061A CN 109046792 A CN109046792 A CN 109046792A
- Authority
- CN
- China
- Prior art keywords
- bubble
- flow type
- mixed flow
- type microbubble
- microbubble generator
- 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.)
- Granted
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D1/00—Flotation
- B03D1/14—Flotation machines
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D1/00—Flotation
- B03D1/02—Froth-flotation processes
- B03D1/025—Froth-flotation processes adapted for the flotation of fines
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Biotechnology (AREA)
Abstract
The invention discloses a kind of mixed flow type microbubble generators, including the collapsible tube, trunnion and diffuser being sequentially connected to, the output end of the diffuser is docked with efferent duct, the input end of the collapsible tube is docked with closed gas-liquid mixed room, the gas-liquid mixed room is equipped with pressed gas air inlet pipe and fluid injection pipe, is equipped with helical blade in the efferent duct.The invention also discloses a kind of bubble distributers comprising above-mentioned microvesicle generators.The present invention combines high pressure solution air elutriation and goes out the method that method and Venturi tube jet stream are formed at two kinds of microvesicles of bubble, and bubble is further broken up using helical blade, a large amount of diameters can be formed in the microvesicle of 0.1-0.3mm, being formed by bubble has the characteristics that bubble size is smaller, dispersion ratio is more uniform, and the adjusting of bubble diameter can be realized by replacing the helical blade of different size, have many advantages, such as that job stability height, nozzle are not easy to plug.
Description
Technical field
The invention belongs to mining equiment flotation technology field more particularly to a kind of mixed flow type microbubble generators and bubble distribution
Device.
Background technique
Flotation is the important channel for recycling valuable mineral in nonferrous metallic ores, and flotation column has compared to other floatation equipments
High concentration ratio, equipment are installed and the lot of advantages such as maintenance is simple, production process is easily controllable, especially sorts to fine mineral particle
It is with the obvious advantage, gradually develop into the main floatation equipment of nonferrous metal mine.Bubble is the indispensable key of froth flotation
Factor, an effective bubble generator should can generate tiny and uniform bubble under maximum possible aeration quantity.
Therefore, the research of flotation column bubble generator is one of most important aspect of flotation column research.
Flotation column bubble generator is divided into internal foam maker and external foam maker according to bubble occurring mode.Internal foam maker
It common are standpipe foam maker, filtering disc type foam maker, gravel bed foam maker etc., but these foam makers easily occur in production
Fouling, blocking often result in flotation column and are not normally functioning, thus seldom use now, the big measurement of external microvesicle generators at present
Become mainstream for internal microvesicle generators.The foaming processes that external bubble generator uses usually have electrolysis method, pressure dissolution
Method and mechanical bubble revulsion etc., external bubble generator solves the problems, such as that foam maker is susceptible to plugging, and industrially obtains wide
General application.Static mixer can air self-suction and aeration quantity it is big, the size of bubble can be manually adjusted, do not blocked without clear
Reason, but its structure is complex, and internal structure requirement on machining accuracy is very high；Swirler type bubble generator is not easy to plug, and works as gas
When steeping generator work, flotation column liquid level is more stable, when flotation column does not work, does not need to exclude extra ore pulp, but the gas
It is uneven to steep generator bubble distribution, and with segregation phenomena；The bubble diameter that self-suction microbubble generator generates is small, but its is right
It is passed through the more demanding of gas, work is not sufficiently stable.
Chinese invention patent 201610467816.4 discloses a kind of fine flotation electrolysis microvesicle generators.But
Above-mentioned microvesicle generators using electrolysis foaming, electrolysis foaming is at high cost, electrode life is limited, replacement electrode cost equally compared with
Height, and it is electrolysed the oxygen generated and hydrogen belongs to extremely incendive gas, there are larger security risks in use process！Its institute
The bubble of generation includes hydrogen, oxygen and general air bubble, these three bubbles are due to density difference, in Mineral Floating Process
Also can be different to the adhesion strength of particle, this influences whether the flotation of mineral grain to a certain extent.
Summary of the invention
The application aims to solve at least one of the technical problems existing in the prior art.For this purpose, an object of the present invention
It is to provide a kind of mixed flow type microbubble generator and bubble distributer, which can form that bubble size is small, dispersion
Uniform microvesicle, and job stability is high.
In order to solve the above technical problems, the present invention adopts the following technical scheme:
A kind of mixed flow type microbubble generator, including the collapsible tube, trunnion and diffuser being sequentially connected to, the diffuser
Output end is docked with efferent duct, and the input end of the collapsible tube is docked with closed gas-liquid mixed room, on the gas-liquid mixed room
Equipped with pressed gas air inlet pipe and fluid injection pipe, helical blade is equipped in the efferent duct.
Further, the axis of the fluid injection pipe is overlapped with the axis of the trunnion, the fluid injection pipe and institute
Air inlet pipe is stated to arrange in angle.
Further, the size of the angle is 40~45 °.
Further, the cone angle of the collapsible tube is 30~35 °.
Further, the cone angle of the diffuser is 35~40 °.
Further, the longitudinal length ratio of the collapsible tube, trunnion and diffuser is 1:4:2.
Further, the spout of the fluid injection pipe is the conical nozzle that cone angle is 15~20 °.
A kind of bubble distributer, at least two annular gas distribution pipes including being arranged concentrically and being connected by connecting tube and
Several above-mentioned mixed flow type microbubble generators are evenly equipped with venthole on the tube wall of each annular gas distribution pipe, are located at outermost ring
It is symmetrically arranged on shape gas distribution pipe and corresponds the air inlet being connected to each efferent duct.
Further, adjacent annular gas distribution pipe, which passes through, is located at several connecting tubes companies uniformly distributed between the two and in a ring
It is logical.
Compared with prior art, the invention has the following beneficial effects:
1. combining high pressure solution air elutriation goes out the method that method and Venturi tube jet stream are formed at two kinds of microvesicles of bubble, it is formed by micro-
Bubble has bubble size smaller, and dispersion is relatively uniform, and has structure simple, and job stability is high, and nozzle is not easy to plug
Advantage can also add foaming agent in water flow.
2. the helical blade being equipped in efferent duct can further break up bubble, a large amount of diameters can be formed in 0.1-
The microvesicle of 0.3mm, and the adjusting of bubble diameter can be realized by replacing the helical blade of different size.
3. mixed flow microvesicle can be uniformly and stably distributed in flotation column cylinder by bubble distributer, be conducive in floatation equipment
The efficient mineralization of bubble and mineral.
Detailed description of the invention
Fig. 1 is invention mixed flow type microbubble generator structural schematic diagram；
Fig. 2 is that bubble distributer of the present invention is mounted on the structural schematic diagram on flotation column.
Specific embodiment
Following will be combined with the drawings in the embodiments of the present invention, and technical solution in the embodiment of the present invention carries out clear, complete
Site preparation description, it is clear that described embodiments are only a part of the embodiments of the present invention, instead of all the embodiments.It is based on
Embodiment in the present invention, it is obtained by those of ordinary skill in the art without making creative efforts every other
Embodiment shall fall within the protection scope of the present invention.
Referring to Fig. 1, a kind of mixed flow type microbubble generator, including tube body 1, tube body 1 include collapsible tube 5, the larynx being sequentially communicated
Pipe 6 and diffuser 7, the outlet of diffuser 7 are connected with efferent duct 9, and the import of collapsible tube 5 and closed gas-liquid mixed room 4 are direct
Connection, gas-liquid mixed room 4 are equipped with gas-pressurized air inlet pipe 2 and fluid injection pipe 3.
The course of work of microvesicle generators is as follows: the fluid sprayed at a high speed from fluid injection pipe 3 introduces gas-liquid mixed room 4
In, make to form negative pressure in gas-liquid mixed room 4, high pressure draught is injected into gas-liquid mixed room 4 through air inlet pipe 2, due to water flow high speed
It moves there are huge pressure difference between the negative pressure generated and high pressure gas, gas is entered in water body by a large amount of dissolutions, and water flow exists
Since the diminution of tube body cross section causes pressure gradually to convert to kinetic energy at collapsible tube 5, flow velocity is accelerated, and gas and liquid two phases are being shunk
Pipe forms strong turbulent fluctuation energy, and gas is sheared, torn by turbulent flow, blending forms a large amount of minor diameter bubbles, and further in larynx
It is mixed in pipe 6, exchanging for violent quality and energy occurs for fluid and gas, and completes gas-liquid in the exit of trunnion 6
The energy transfer process of decentralized medium, in diffuser 7, gas and liquid two phases carry out mutual mass transfer, pass energy, due to diffuser cross
The unexpected increase in section, leads to flows decrease, and the kinetic energy of gas-liquid mixed stream gradates as pressure energy, and bubble is further dispersed into
For the smaller microvesicle of diameter, while the gas dissolved in water body further dissolves out, and a large amount of microvesicles are formed in diffuser.
The present embodiment combines high pressure solution air elutriation and goes out the method that method and Venturi tube jet stream are formed at two kinds of microvesicles of bubble, institute's shape
At bubble have the characteristics that bubble size is smaller, dispersion ratio is more uniform, and can be by adjusting hydraulic pressure and air pressure, replacement not
The spiral clipper of same specification realizes the adjusting of bubble diameter, has many advantages, such as that job stability height, nozzle are not easy to plug.With biography
System Venturi tube acts on molten gas by self-priming and compares, and there are huge pressures between the negative pressure that water flow high-speed motion generates and high pressure gas
Power is poor, and gas is entered in water body by a large amount of dissolutions, and the gas of these dissolutions can largely be precipitated in diffuser, in addition, by height
Addition foaming agent can also further increase bubble effect in pressure water source.
Invention the present embodiment mixed flow type microbubble generator is equipped with helical blade in efferent duct, and helical blade is removably pacified
In efferent duct and coaxially setting.The major diameter of helical blade and the ratio of path are 2:1, and lead angle is 25~30 °,
Screw pitch is 5~10mm.Gas-liquid mixed stream can rotate automatically to form the turbulent flow of rotation along the hand of spiral by helical blade,
The turbulent flow further shears bubble, further realizes the refinement of bubble, and bubble size is stablized in 0.1-0.3mm, and can be with
Helical blade by replacing different size realizes the adjusting of bubble diameter.
Specifically, the axis of fluid injection pipe 3 is overlapped with the axis of trunnion 6, by above-mentioned setting can collapsible tube 5,
The stable flow field that is evenly distributed is generated in trunnion 6 and diffuser 7, on the one hand can be formed stable active force to gas, be obtained
Diameter is distributed more uniform bubble, on the other hand can also reduce fluid when by trunnion and the friction of tube wall, reduce edge
Journey energy loss improves energy conversion efficiency.
Preferably, the injection direction of fluid injection pipe 3 intersects with the injection direction of air inlet pipe 2 and there are certain angle,
Corner dimension is preferably 40~45 °.Air inlet pipe 2 is a certain included angle with trunnion central axes, is conducive to the transverse flow for increasing gas
Speed can increase the collision shear force of turbulent flow and gas at collapsible tube, be conducive to the dispersion of gas.
It preferably, is further bubble disintegration, the longitudinal section of collapsible tube 5 and diffuser is taper.Wherein, collapsible tube
5 cone angle is 30~35 °, and the cone angle of diffuser 7 is 35~40 °, collapsible tube 5, trunnion 6, diffuser 7 longitudinal length ratio be
1:4:2, the spout of fluid injection pipe 3 are the conical nozzle that cone angle is 15~20 °, and efferent duct 8 is equal diameter pipeline and its internal diameter
Equal with the exit internal diameter of diffuser 7, by above-mentioned setting, bubble size can be refined further.
Referring to fig. 2, a kind of bubble distributer, including at least two annulars for being arranged concentrically and being connected by connecting tube 10
Gas distribution pipe 11 and several above-mentioned mixed flow type microbubble generators, it is each annular gas distribution pipe 11 tube wall on be evenly equipped with venthole, be located at
Circular symmetric is equipped with the air inlet being connected to each efferent duct 9 one-to-one correspondence and (does not show in figure on outermost annular gas distribution pipe 11
Out).
Specifically, this implementation, using two annular gas distribution pipes 11, the diameter ratio of two annular gas distribution pipes 11 is 1:2, connection
Pipe 10 is evenly arranged in the annular space between two annular gas distribution pipes, is set on outermost layer annular gas distribution pipe 11 there are four air inlet,
To being connected to a bubble distributer on each air inlet.In practical applications, this bubble distributer is paid the utmost attention to be applied to floating
It selects on column, annular gas distribution pipe is arranged in flotation column, and 4 mixed flow type microbubble generators are mounted on the side wall of flotation column cylinder 12
And be connected to the air inlet on annular gas distribution pipe, pressurised stream enters from the fluid injection pipe of mixed flow type microbubble generator, adds
It presses air to enter from the air inlet pipe of mixed flow type microbubble generator, forms a large amount of micro-bubbles at diffuser, bubble passes through air inlet
Mouth enters shape gas distribution pipe, and is sprayed by the venthole on shape gas distribution pipe, and formation is evenly distributed stable in flotation column cylinder
Rise bubble.
Above-described embodiment is only to clearly demonstrate examples made by the present invention, rather than the restriction to embodiment.For
For those of ordinary skill in the art, other various forms of variations or change can also be made on the basis of the above description
It is dynamic.Here without can not be also exhaustive to all embodiments.And the obvious variation or change thus amplified out
It is dynamic to be still in the protection scope of this invention.
Claims (9)
1. a kind of mixed flow type microbubble generator, including the collapsible tube, trunnion and diffuser being sequentially connected to, the diffuser it is defeated
Outlet is docked with efferent duct, it is characterised in that: the input end of the collapsible tube is docked with closed gas-liquid mixed room, the gas-liquid
Mixing chamber is equipped with pressed gas air inlet pipe and fluid injection pipe, is equipped with helical blade in the efferent duct.
2. mixed flow type microbubble generator according to claim 1, it is characterised in that: the axis of the fluid injection pipe and institute
The axis for stating trunnion is overlapped, and the fluid injection pipe and the air inlet pipe are arranged in angle.
3. mixed flow type microbubble generator according to claim 2, it is characterised in that: the size of the angle is 40~45 °.
4. mixed flow type microbubble generator according to claim 1 or 2, it is characterised in that: the cone angle of the collapsible tube is 30
~35 °.
5. mixed flow type microbubble generator according to claim 1 or 2, it is characterised in that: the cone angle of the diffuser is 35
~40 °.
6. mixed flow type microbubble generator according to claim 1 or 2, it is characterised in that: the collapsible tube, trunnion and expansion
The longitudinal length ratio of separate tube is 1:4:2.
7. mixed flow type microbubble generator according to claim 1 or 2, it is characterised in that: the spout of the fluid injection pipe
The conical nozzle for being 15~20 ° for cone angle.
8. a kind of bubble distributer, it is characterised in that: including at least two annulars for being arranged concentrically and being connected by connecting tube
Gas distribution pipe and several described in any item mixed flow type microbubble generators of claim 1-7, the tube wall of each annular gas distribution pipe
On be evenly equipped with venthole, on outermost annular gas distribution pipe annular be equipped with corresponded with each efferent duct be connected into
Port.
9. bubble distributer according to claim 8, it is characterised in that: adjacent annular gas distribution pipe, which passes through, to be located between the two
And uniformly distributed several connecting tubes connections in a ring.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811244061.7A CN109046792B (en) | 2018-10-24 | 2018-10-24 | Mixed-flow type microbubble generator and bubble distributor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811244061.7A CN109046792B (en) | 2018-10-24 | 2018-10-24 | Mixed-flow type microbubble generator and bubble distributor |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN109046792A true CN109046792A (en) | 2018-12-21 |
| CN109046792B CN109046792B (en) | 2020-09-08 |
Family
ID=64765532
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201811244061.7A Active CN109046792B (en) | 2018-10-24 | 2018-10-24 | Mixed-flow type microbubble generator and bubble distributor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN109046792B (en) |
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109704447A (en) * | 2019-03-05 | 2019-05-03 | 苏州方舟环保科技有限公司 | A kind of urban river water acid-base accommodation device |
| CN109908712A (en) * | 2019-04-24 | 2019-06-21 | 攀钢集团钛业有限责任公司 | The air and liquid mixer absorbed for titanium tetrachloride |
| CN110193429A (en) * | 2019-05-23 | 2019-09-03 | 三门峡亚太科技有限公司 | A kind of ultralow grade alumyte waste residue is without transmission bulk flotation device and floatation process |
| CN110479127A (en) * | 2019-07-18 | 2019-11-22 | 中国矿业大学 | A kind of micro-nano bubble generating device and the method for generating micro-nano bubble |
| CN110947525A (en) * | 2019-12-16 | 2020-04-03 | 李宾 | Nanobubble flotation column |
| CN111036107A (en) * | 2019-12-31 | 2020-04-21 | 苏州思诚者信息科技有限公司 | Supergravity micro-nano bubble generator and generating system |
| CN111081609A (en) * | 2019-12-26 | 2020-04-28 | 西安奕斯伟硅片技术有限公司 | Cleaning and etching system |
| CN111663040A (en) * | 2020-06-22 | 2020-09-15 | 中南大学 | Method for enhancing oxygen oxidation iron removal in solution by using microbubble generator |
| WO2020193845A1 (en) * | 2019-03-22 | 2020-10-01 | Hilla Consulting Oy | A fluid suspension tube |
| CN112808476A (en) * | 2019-11-15 | 2021-05-18 | 中国石油天然气集团有限公司 | Nozzle atomization effect strengthening device and nozzle |
| CN114642978A (en) * | 2022-03-22 | 2022-06-21 | 浙江一龙环保科技有限公司 | Suction type rotational flow microbubble generator |
Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6312230B1 (en) * | 1998-04-17 | 2001-11-06 | Evgueni D. Petroukhine | Liquid-gas jet apparatus variants |
| CN201384946Y (en) * | 2009-03-24 | 2010-01-20 | 山东东岳有机硅材料有限公司 | Gas distributor for fluidized bed reactor |
| CN103464057A (en) * | 2013-09-06 | 2013-12-25 | 天津聚贤达科技有限公司 | Novel gas distributor |
| CN103861511A (en) * | 2014-02-19 | 2014-06-18 | 中国矿业大学 | Mining porous spiral-type foam generating device |
| CN104632216A (en) * | 2015-01-16 | 2015-05-20 | 中国矿业大学 | Rotary jet self-priming type short-range strengthening foam production device for dust suppression of coal mining machine |
| CN205779946U (en) * | 2016-07-05 | 2016-12-07 | 江苏华电仪征热电有限公司 | A kind of mjector |
| CN106824020A (en) * | 2017-02-23 | 2017-06-13 | 北京神雾环境能源科技集团股份有限公司 | For the distribution device in gas-fluid and paste state bed reactor of paste state bed reactor |
| JP2017189733A (en) * | 2016-04-12 | 2017-10-19 | 大生工業株式会社 | Fine bubble generator |
| CN206730898U (en) * | 2017-04-08 | 2017-12-12 | 深圳欧威奇科技有限公司 | Jet mixer with inside spin |
-
2018
- 2018-10-24 CN CN201811244061.7A patent/CN109046792B/en active Active
Patent Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6312230B1 (en) * | 1998-04-17 | 2001-11-06 | Evgueni D. Petroukhine | Liquid-gas jet apparatus variants |
| CN201384946Y (en) * | 2009-03-24 | 2010-01-20 | 山东东岳有机硅材料有限公司 | Gas distributor for fluidized bed reactor |
| CN103464057A (en) * | 2013-09-06 | 2013-12-25 | 天津聚贤达科技有限公司 | Novel gas distributor |
| CN103861511A (en) * | 2014-02-19 | 2014-06-18 | 中国矿业大学 | Mining porous spiral-type foam generating device |
| CN104632216A (en) * | 2015-01-16 | 2015-05-20 | 中国矿业大学 | Rotary jet self-priming type short-range strengthening foam production device for dust suppression of coal mining machine |
| JP2017189733A (en) * | 2016-04-12 | 2017-10-19 | 大生工業株式会社 | Fine bubble generator |
| CN205779946U (en) * | 2016-07-05 | 2016-12-07 | 江苏华电仪征热电有限公司 | A kind of mjector |
| CN106824020A (en) * | 2017-02-23 | 2017-06-13 | 北京神雾环境能源科技集团股份有限公司 | For the distribution device in gas-fluid and paste state bed reactor of paste state bed reactor |
| CN206730898U (en) * | 2017-04-08 | 2017-12-12 | 深圳欧威奇科技有限公司 | Jet mixer with inside spin |
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109704447A (en) * | 2019-03-05 | 2019-05-03 | 苏州方舟环保科技有限公司 | A kind of urban river water acid-base accommodation device |
| WO2020193845A1 (en) * | 2019-03-22 | 2020-10-01 | Hilla Consulting Oy | A fluid suspension tube |
| CN109908712A (en) * | 2019-04-24 | 2019-06-21 | 攀钢集团钛业有限责任公司 | The air and liquid mixer absorbed for titanium tetrachloride |
| CN109908712B (en) * | 2019-04-24 | 2024-04-02 | 攀钢集团钛业有限责任公司 | Gas-liquid mixer for titanium tetrachloride absorption |
| CN110193429A (en) * | 2019-05-23 | 2019-09-03 | 三门峡亚太科技有限公司 | A kind of ultralow grade alumyte waste residue is without transmission bulk flotation device and floatation process |
| CN110479127A (en) * | 2019-07-18 | 2019-11-22 | 中国矿业大学 | A kind of micro-nano bubble generating device and the method for generating micro-nano bubble |
| CN112808476A (en) * | 2019-11-15 | 2021-05-18 | 中国石油天然气集团有限公司 | Nozzle atomization effect strengthening device and nozzle |
| CN110947525A (en) * | 2019-12-16 | 2020-04-03 | 李宾 | Nanobubble flotation column |
| CN111081609A (en) * | 2019-12-26 | 2020-04-28 | 西安奕斯伟硅片技术有限公司 | Cleaning and etching system |
| CN111036107A (en) * | 2019-12-31 | 2020-04-21 | 苏州思诚者信息科技有限公司 | Supergravity micro-nano bubble generator and generating system |
| CN111663040A (en) * | 2020-06-22 | 2020-09-15 | 中南大学 | Method for enhancing oxygen oxidation iron removal in solution by using microbubble generator |
| CN114642978A (en) * | 2022-03-22 | 2022-06-21 | 浙江一龙环保科技有限公司 | Suction type rotational flow microbubble generator |
| CN114642978B (en) * | 2022-03-22 | 2023-01-10 | 浙江一龙环保科技有限公司 | Suction type rotational flow microbubble generator |
Also Published As
| Publication number | Publication date |
|---|---|
| CN109046792B (en) | 2020-09-08 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN109046792A (en) | A kind of mixed flow type microbubble generator and bubble distributer | |
| CN107744732B (en) | Tubular micro-bubble generator | |
| CN209020581U (en) | A kind of mixed flow type microbubble generator and bubble distributer | |
| CN110479127A (en) | A kind of micro-nano bubble generating device and the method for generating micro-nano bubble | |
| CN103480501B (en) | Phosphate ore floatation method and system | |
| CN110947525B (en) | Nanobubble flotation column | |
| CN111821871A (en) | Micro-nano bubble generator with composite cutting function | |
| CN111617656B (en) | Micro-bubble generator serving as atomizer and using method thereof | |
| CN110877294B (en) | High-negative-pressure micro-nano bubble enhanced abrasive flow cavitation polishing device and method | |
| CN107159471B (en) | Has ore pulp from driving and the floatation equipment of self-priming airway dysfunction | |
| CN112264198A (en) | Micro-nano bubble flotation machine | |
| CN112535988A (en) | Micro-nano bubble preparation device and preparation method thereof | |
| CN209005563U (en) | A kind of double fluid head-on collision micro-nano bubble generator of jetting type | |
| KR101865240B1 (en) | Device for generating bubble | |
| CN109939840B (en) | Forced turbulence mineralization reaction device and method | |
| CN110898698B (en) | Microbubble generator and gas-liquid reactor comprising same | |
| CN201737717U (en) | Ultra-micron air bubble spray head | |
| CN115254444B (en) | Cavitation water jet grinding and floating device and grinding and floating method | |
| CN117550728A (en) | Self-priming micro-nano bubble generation device and generation method | |
| CN217795537U (en) | Microbubble generator and multiphase reactor | |
| CN212017421U (en) | Micro-bubble generator | |
| CN215876939U (en) | Jet flow mixing nozzle | |
| CN211800086U (en) | Micro-nano bubble generator with composite cutting function | |
| CN109987726A (en) | A kind of breaking micro-nano bubble method for generation of multistage rotary-cut and device | |
| CN116020665A (en) | Fluidized coarse grain flotation device and method capable of adjusting water-gas flow field and turbulence |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant |