CN106474950A - A kind of Liqiud-gas mixing device - Google Patents
A kind of Liqiud-gas mixing device Download PDFInfo
- Publication number
- CN106474950A CN106474950A CN201610933315.0A CN201610933315A CN106474950A CN 106474950 A CN106474950 A CN 106474950A CN 201610933315 A CN201610933315 A CN 201610933315A CN 106474950 A CN106474950 A CN 106474950A
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- CN
- China
- Prior art keywords
- gas
- liquid
- pipeline
- liqiud
- transfer pipeline
- 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.)
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Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/20—Mixing gases with liquids
- B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/20—Mixing gases with liquids
- B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
- B01F23/2366—Parts; Accessories
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F2025/91—Direction of flow or arrangement of feed and discharge openings
- B01F2025/919—Direction of flow or arrangement of feed and discharge openings characterised by the disposition of the feed and discharge openings
- B01F2025/9191—Direction of flow or arrangement of feed and discharge openings characterised by the disposition of the feed and discharge openings characterised by the arrangement of the feed openings for one or more flows, e.g. for the mainflow and the flow of an additional component
- B01F2025/919125—Direction of flow or arrangement of feed and discharge openings characterised by the disposition of the feed and discharge openings characterised by the arrangement of the feed openings for one or more flows, e.g. for the mainflow and the flow of an additional component with feed openings in the center and at the circumference of the main flow
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
Abstract
The present invention provides a kind of Liqiud-gas mixing device, including gas transfer pipeline, liquid transmission pipeline, air accumulation chamber, gas-liquid mixed rod and blending transportation passage；Gas transfer pipeline and liquid transmission pipeline are arranged at an angle of 90, and gas transfer pipeline and liquid transmission pipeline are all pipe, have an annular air accumulation chamber between gas transfer pipeline and liquid transmission pipeline；Gas-liquid mixed rod is circular tube structure, is arranged in the pipeline that liquid transmission pipeline overlaps with gas transfer pipeline, and the side of the excellent pipe of gas-liquid mixed is uniformly distributed multiple apertures identical and gives vent to anger circular hole, and the perforate direction of circular hole of giving vent to anger is identical with the direction of motion of liquid；The gas of air accumulation intracavity is mixed with liquid by gas-liquid mixed rod；And by be connected with liquid transmission pipeline and parallel blending transportation passage output, during mixing, the flow direction of gas is consistent with the flow direction of liquid.So make more steady when gas and liquid mixing, improve mixing efficiency.
Description
Technical field
The present invention relates to a kind of mixing arrangement field, particularly to a kind of Liqiud-gas mixing device.
Background technology
In recent decades, due to traditional industry and infant industry, such as Chemical Engineering, metallurgical engineering, nuclear engineering, aviation and boat
Developing rapidly of its engineering etc., promotes research and the application of two-phase flow, is that it develops into an independent research branch,
Obtain extensive attention.But, due to the limitation of intrinsic complexity, multiformity and measurement means, up to the present,
Either in theory, or in method, this research is in developmental stage, and, in from now on longer time,
To continue to be one that each airs his own views, tentative strong, it is filled with chance and the sphere of learning breaking through.
Biphase gas and liquid flow is the most universal a kind of form in multiphase flow, is widely present in each industrial processes
In, national economy and daily life play very important effect.For example, the boiler in energy source and power industrial process, change
The equipment such as the reboiler in hot device, steam-water separator and chemical industry process, condenser, the steam in refrigeration low-temperature industrial process
During oil-gas mining in compression refrigeration equipment, and petroleum industry, oil and gas multiphase flow etc., all there is biphase gas and liquid flow kinetoplast
System.Additionally, with the development of space technology, in microgravity condition such as the satellite of aerospace field, space station and space platforms
Under equipment in, there is also biphase gas and liquid flow.
There is gas-liquid delivery, in order to ensure the normal operation of multiphase pipeline it is necessary to mix in the pipeline of practical engineering application
Defeated pump intake installs air and liquid mixer, makes gas-liquid uniform inflow as far as possible；Exist in unit equipment reaction between gas-liquid two-phase,
Absorb, extraction, dissolving and the process such as emulsifying, these technical processs all need by gas-liquid two-phase between mixed process to realize, be
Raising mixing efficiency, must be provided with Liqiud-gas mixing device in flow process.Liqiud-gas mixing device seems very heavy in two phase flow
Will.
Existing patent No. CN204563382U, a kind of patent of title " air and liquid mixer " proposes：A kind of air and liquid mixer,
Including mixer case, mixer outlet joint, flow-disturbing dividing plate and two flow-disturbing springs；The diameter of mixing section and breeze way
Diameter be all higher than the diameter of contraction section；Mixer outlet joint rotating connection is on the foam outlet of mixer case, and is mixing
It is provided with sealing ring at device outlet connection and the end contact of mixer case；The outer wall of mixer case is provided with and mixing section phase
Logical inlet.But this patented technology yet suffers from following two problems：First, this patented technology adopts at one to gas
Mixed with liquid, and the method being provided without multiple spot mixing, mixed uniformly effect can not be reached；Second, this patent skill
When art gas and liquid mixing, gas motion direction and liquid motion direction are orthogonal, can change in mixed process
Gas and the original direction of motion of liquid, do not utilize the motion of mixed gas-liquid mixture.
Existing patent No. CN 203425729 U, the patent of title " air and liquid mixer " proposes：A kind of air and liquid mixer, its
There is water inlet, air inlet and outlet, between water inlet and outlet, be provided with hybrid chamber, wherein, water inlet and hybrid chamber it
Between be provided with inlet opening, the valve rod of a needle-valve passes through inlet opening, and valve rod is in frustum near the part of water inlet, the frustum of valve rod
Partial cross-sectional area is gradually increased from away from water inlet one end to the one end near water inlet.But this patented technology is still
There are following two problems：First, this patented technology is using mixing to gas and liquid at one, and it is provided without multiple spot mixing
Method, mixed uniformly effect can not be reached.
For above-mentioned deficiency, the present inventor has invented " a kind of Liqiud-gas mixing device ", enables gas and liquid
Equably mixed, improve the efficiency of mixing.
Content of the invention
The technical problem to be solved is, for above-mentioned problem, to provide a kind of Liqiud-gas mixing device,
Improve the independence of device, improve mixing homogeneity further so that gas-liquid material mixing become standardization, homogenization and
Controlledization, and then improve mixed effect.
The main object of the present invention is to provide a kind of Liqiud-gas mixing device, realizes the uniform mixing of gas and liquid.This
Bright technical scheme is：
A kind of Liqiud-gas mixing device, including gas transfer pipeline, liquid transmission pipeline, air accumulation chamber, gas-liquid mixed rod
With blending transportation passage；
Described gas transfer pipeline and liquid transmission pipeline are arranged at an angle of 90, and gas transfer pipeline and liquid transmission pipeline are complete
For pipe, between gas transfer pipeline and liquid transmission pipeline, there is an annular air accumulation chamber；
Described gas-liquid mixed rod is circular tube structure, is arranged on the pipeline that liquid transmission pipeline is overlapped with gas transfer pipeline
Interior, one end of gas-liquid mixed rod is connected with air accumulation chamber and no seals for gas feed, and the other end seals, in gas-liquid mixed
The side of excellent pipe is uniformly distributed multiple apertures identical and gives vent to anger circular hole, the perforate direction of circular hole of giving vent to anger and the direction of motion of liquid
Identical；The gas of air accumulation intracavity is mixed with liquid by gas-liquid mixed rod；And by being connected with liquid transmission pipeline
Logical and parallel blending transportation passage output, during mixing, the flow direction of gas is consistent with the flow direction of liquid.
In such scheme, described gas-liquid mixed rod divides three groups to be axially distributed along liquid flow direction, each group of gas-liquid mixed
The quantity of rod is the six roots of sensation, and six roots of sensation gas-liquid mixed rod is symmetrically arranged along pipeline circumference.
In such scheme, described air accumulation chamber is the cylinder class formation being enclosed within outside liquid transmission pipeline, air accumulation
Chamber outboard structure and liquid transmission pipeline are by the way of welding.
In such scheme, described liquid transmission pipeline horizontal positioned when mounted, gas transfer pipeline is vertically put when installing
Put, gas from top to bottom enters air accumulation chamber.
In such scheme, it is wound around by extruded polystyrene foam outside described gas transfer pipeline and liquid transmission pipeline
The insulation material of plastics composition.
In such scheme, the internal diameter D of described gas transfer pipeline1, gas-liquid mixed rod internal diameter D2Go out with gas-liquid mixing rod
Gas Circularhole diameter D3Ratio is D1：D2：
In such scheme, the liquid delivery end of described liquid transmission pipeline is provided with liquid delivery end adpting flange.
In such scheme, the inlet end of described gas transfer pipeline is provided with gas transfer pipeline adpting flange.
In such scheme, the port of export of described blending transportation passage is provided with blending transportation passage adpting flange.
Compared with prior art, beneficial effects of the present invention are：Air accumulation chamber of the present invention is to be enclosed within liquid transmission pipeline
The cylinder class formation in outside, and there is good sealing, for storing gas.Put when mounted by level for liquid transmission pipeline
Put, gas transfer pipeline is disposed vertically when installing, and makes gas from top to bottom enter air accumulation chamber.The gas entering accumulation chamber leads to
Cross the gas-liquid mixed rod being distributed on liquid transmission pipeline inwall to realize and equably the mixing in the same direction of liquid.The present invention improves
The independence of device, improves mixing homogeneity further so that the mixing of gas-liquid material becomes standardization, homogenization and controlled
Change, and then improve mixed effect.
Brief description
Fig. 1 is the air and liquid mixer sectional view of an embodiment of the present invention；
Fig. 2 is A-A or B-B or C-C view in Fig. 1 air and liquid mixer；
Fig. 3 is the I partial enlarged view in Fig. 1 air and liquid mixer.
In figure, 1- liquid delivery end adpting flange；2- liquid delivery end；3- liquid transmission pipeline；4- air accumulation chamber；5-
Gas transfer pipeline；6- gas transfer pipeline adpting flange；7- gas-liquid mixed rod；8- blending transportation passage；9- blending transportation leads to
Road adpting flange；10- gives vent to anger circular hole；The direction of arrow represents the flow direction of gas or liquid；D1In-gas transfer pipeline
Footpath；D2The internal diameter of-gas-liquid mixed rod；D3Give vent to anger Circularhole diameter on-gas-liquid mixed rod.
Specific embodiment
The present invention provides a kind of Liqiud-gas mixing device, improves the independence of device, improves mixing homogeneity further,
Make the mixing of gas-liquid material become standardization, homogenization and controlledization, and then improve mixed effect.Below in conjunction with the accompanying drawings to this
Bright it is described in further detail.
The main object of the present invention is to provide a kind of Liqiud-gas mixing device, realizes the uniform mixing of gas and liquid.Fig. 1 institute
It is shown as a kind of embodiment of Liqiud-gas mixing device of the present invention, described Liqiud-gas mixing device includes liquid delivery end 2, liquid
Transfer pipeline 3, air accumulation chamber 4, gas transfer pipeline 5, gas-liquid mixed rod 7 and blending transportation passage 8.Described gas input
Pipeline 5 and liquid transmission pipeline 3 are arranged at an angle of 90, and gas transfer pipeline 5 and liquid transmission pipeline 3 are all pipe, and gas conveys
There is an annular air accumulation chamber 4 between pipeline 5 and liquid transmission pipeline 3.The liquid delivery end of described liquid transmission pipeline 3
2 are provided with liquid delivery end adpting flange 1, and the inlet end of described gas transfer pipeline 5 is provided with gas transfer pipeline adpting flange 6,
The port of export of described blending transportation passage 8 is provided with blending transportation passage adpting flange 9.
Gas-liquid mixed rod 7 is circular tube structure, and one end is connected with air accumulation chamber and no seals, the other end for gas feed
Sealing, is uniformly distributed multiple apertures identical in pipe side and gives vent to anger circular hole 10, the perforate direction of circular hole 10 of giving vent to anger and liquid
The direction of motion identical.7 points three groups of gas-liquid mixed rod is axially distributed along liquid flow direction, between three groups of gas-liquid mixed rods 7 between
Every a certain distance, each group of gas-liquid mixed rod 7 is made up of six roots of sensation gas-liquid mixed rod, and six roots of sensation gas-liquid mixed rod 7 is defeated along liquid
Pipeline 3 circumference is sent symmetrically to arrange, as shown in Figure 2.Gas in air accumulation chamber 4 passes through multiple on gas-liquid mixed rod 7
Circular hole 10 of giving vent to anger is mixed with liquid, and by being connected with liquid transmission pipeline 3 and parallel blending transportation passage 8 is defeated
Go out, during mixing, the flow direction of gas is consistent with the flow direction of liquid, so make more flat when gas and liquid mixing
Surely, reduce the generation of vibration.
Air accumulation chamber 4 is the cylinder class formation being enclosed within liquid transmission pipeline 3 outside, air accumulation chamber 4 outboard structure with
Liquid transmission pipeline 3 using welding by the way of so as to have good sealing, for storing gas.Liquid transmission pipeline 3 exists
Horizontal positioned during installation, gas transfer pipeline 5 is disposed vertically when installing, and makes gas from top to bottom enter air accumulation chamber 4.Enter
The gas of accumulation chamber 4 is realized and equably the mixing in the same direction of liquid by the gas-liquid mixed that is distributed on liquid transmission pipeline 3 rod 7
Close.On gas-liquid mixed rod 7 Way out of gas level as shown in Figure 1 to the right, and the flow direction of liquid be also level to the right,
The mode of such arrangement maintains gas and the original kinestate of liquid is more conducive to the steady mixing of gas and liquid, improves
Mixing efficiency.Described gas transfer pipeline 5 and liquid transmission pipeline 3 outside are wound around and are made up of extruded polystyrene foam plasticss
Insulation material, make stablizing of the gas within gas transfer pipeline 5 and liquid transmission pipeline 3 and liquid keeping temperature.
As shown in figure 3, the internal diameter D of described gas transfer pipeline 51, the internal diameter D of gas-liquid mixed rod 72On gas-liquid mixing rod 7
Give vent to anger Circularhole diameter D3Ratio is D1：D2：The Liqiud-gas mixing device meeting this diameter ratio is more conducive to
Gas-liquid mixed uniform, it is to avoid the not enough phenomenon of gas flow, liquid when simultaneously avoiding gas-liquid mixed occur during gas-liquid mixed
Enter the phenomenon of gas transfer pipeline.
The a series of detailed description of those listed above is only for illustrating of the possible embodiments of the present invention,
They simultaneously are not used to limit the scope of the invention, all Equivalent embodiments made without departing from skill spirit of the present invention or change
Should be included within the scope of the present invention.
Claims (9)
1. a kind of Liqiud-gas mixing device it is characterised in that include gas transfer pipeline (5), liquid transmission pipeline (3), gas gather
Collection chamber (4), gas-liquid mixed rod (7) and blending transportation passage (8)；
Described gas transfer pipeline (5) and liquid transmission pipeline (3) are arranged at an angle of 90, and gas transfer pipeline (5) and liquid convey
Pipeline (3) is all pipe, has an annular air accumulation chamber between gas transfer pipeline (5) and liquid transmission pipeline (3)
(4)；
Described gas-liquid mixed rod (7) is circular tube structure, is arranged on what liquid transmission pipeline (3) was overlapped with gas transfer pipeline (5)
In pipeline, one end of gas-liquid mixed rod (7) is connected with air accumulation chamber (4) and no seals for gas feed, and the other end seals,
It is uniformly distributed multiple apertures identical in the side of gas-liquid mixed rod (7) pipe to give vent to anger circular hole (10), the opening of circular hole of giving vent to anger (10)
Hole direction is identical with the direction of motion of liquid；Gas in air accumulation chamber (4) is mixed with liquid by gas-liquid mixed rod (7)
Close；And by be connected with liquid transmission pipeline (3) and parallel blending transportation passage (8) output, the flowing of gas during mixing
Direction is consistent with the flow direction of liquid.
2. Liqiud-gas mixing device according to claim 1 is it is characterised in that three groups of described gas-liquid mixed rod (7) point is along liquid
Body flow direction is axially distributed, and the quantity of each group of gas-liquid mixed rod (7) is the six roots of sensation, and six roots of sensation gas-liquid mixed rod (7) is along pipeline
Circumference is symmetrically arranged.
3. a kind of Liqiud-gas mixing device according to claim 1 is it is characterised in that described air accumulation chamber (4) is to be enclosed within
Cylinder class formation outside liquid transmission pipeline (3), air accumulation chamber (4) outboard structure and liquid transmission pipeline (3) are using weldering
The mode connecing.
4. a kind of Liqiud-gas mixing device according to claim 1 is it is characterised in that described liquid transmission pipeline (3) is in peace
Horizontal positioned during dress, gas transfer pipeline (5) is disposed vertically when installing, and gas from top to bottom enters air accumulation chamber (4).
5. a kind of Liqiud-gas mixing device according to claim 1 is it is characterised in that described gas transfer pipeline (5) and liquid
Body transfer pipeline is wound around, outside (3), the insulation material being made up of extruded polystyrene foam plasticss.
6. a kind of Liqiud-gas mixing device according to claim 1 it is characterised in that described gas transfer pipeline (5) interior
Footpath D1, gas-liquid mixed rod (7) internal diameter D2With the Circularhole diameter D that gives vent to anger on gas-liquid mixing rod (7)3Ratio is
7. a kind of Liqiud-gas mixing device according to claim 1 is it is characterised in that the liquid of described liquid transmission pipeline (3)
Body delivery end (2) is provided with liquid delivery end adpting flange (1).
8. a kind of Liqiud-gas mixing device according to claim 1 is it is characterised in that the entering of described gas transfer pipeline (5)
Gas end is provided with gas transfer pipeline adpting flange (6).
9. a kind of Liqiud-gas mixing device according to claim 1 is it is characterised in that the going out of described blending transportation passage (8)
Mouth end is provided with blending transportation passage adpting flange (9).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610933315.0A CN106474950A (en) | 2016-10-25 | 2016-10-25 | A kind of Liqiud-gas mixing device |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610933315.0A CN106474950A (en) | 2016-10-25 | 2016-10-25 | A kind of Liqiud-gas mixing device |
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| CN106474950A true CN106474950A (en) | 2017-03-08 |
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Family Applications (1)
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|---|---|---|---|
| CN201610933315.0A Pending CN106474950A (en) | 2016-10-25 | 2016-10-25 | A kind of Liqiud-gas mixing device |
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Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107551842A (en) * | 2017-09-28 | 2018-01-09 | 苏州百硕自动化环保设备有限公司 | A kind of gas cleaning decoction continuous mixer structure |
| CN108905661A (en) * | 2018-07-27 | 2018-11-30 | 东北石油大学 | A kind of pipe gas liquid mixer and oil field recharged waste water expose oxygen method |
| CN109675476A (en) * | 2018-12-19 | 2019-04-26 | 西安交通大学 | A kind of vertical cluster the bottom of the channel import bubbly two phase flow mixes device and method |
| CN110201589A (en) * | 2019-05-10 | 2019-09-06 | 清华大学 | A kind of micro-mixer of the dispersant liquid drop in highly viscous fluid or bubble |
| CN110567675A (en) * | 2019-07-24 | 2019-12-13 | 中国空间技术研究院 | Experimental device and method for equivalently implementing gas-liquid distribution in microgravity low-temperature environment |
| CN110917924A (en) * | 2019-12-16 | 2020-03-27 | 肖文婷 | Mixing device for chemical foaming |
| CN114831069A (en) * | 2022-05-31 | 2022-08-02 | 福建省寰杰科技发展有限公司 | Seafood culture pond with seawater retreatment device |
| CN115350426A (en) * | 2022-08-31 | 2022-11-18 | 徐工消防安全装备有限公司 | Fire-fighting foam foaming device, system and foaming method |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1871061A (en) * | 2001-09-14 | 2006-11-29 | 海水充氧景象公司 | Device for oxygenating sea water |
| CN102671558A (en) * | 2012-06-11 | 2012-09-19 | 董兰田 | Water and air sol generator |
| CN102711963A (en) * | 2009-09-03 | 2012-10-03 | 泽农科技合股公司 | Gas sparger for a filtering membrane |
| WO2013008147A2 (en) * | 2011-07-12 | 2013-01-17 | Saipem S.P.A. | Urea reactor tray, reactor, and production process |
| CN204017237U (en) * | 2014-07-31 | 2014-12-17 | 成都自能消防设备有限公司 | A kind of Liqiud-gas mixing device |
| CN204522789U (en) * | 2015-02-12 | 2015-08-05 | 宁波同力泵业有限公司 | Multi-point injection air and liquid mixer |
| CN104884394A (en) * | 2012-10-25 | 2015-09-02 | 三菱丽阳株式会社 | Aeration device, operation method therefor, and water treatment apparatus |
-
2016
- 2016-10-25 CN CN201610933315.0A patent/CN106474950A/en active Pending
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1871061A (en) * | 2001-09-14 | 2006-11-29 | 海水充氧景象公司 | Device for oxygenating sea water |
| CN102711963A (en) * | 2009-09-03 | 2012-10-03 | 泽农科技合股公司 | Gas sparger for a filtering membrane |
| WO2013008147A2 (en) * | 2011-07-12 | 2013-01-17 | Saipem S.P.A. | Urea reactor tray, reactor, and production process |
| CN102671558A (en) * | 2012-06-11 | 2012-09-19 | 董兰田 | Water and air sol generator |
| CN104884394A (en) * | 2012-10-25 | 2015-09-02 | 三菱丽阳株式会社 | Aeration device, operation method therefor, and water treatment apparatus |
| CN204017237U (en) * | 2014-07-31 | 2014-12-17 | 成都自能消防设备有限公司 | A kind of Liqiud-gas mixing device |
| CN204522789U (en) * | 2015-02-12 | 2015-08-05 | 宁波同力泵业有限公司 | Multi-point injection air and liquid mixer |
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107551842A (en) * | 2017-09-28 | 2018-01-09 | 苏州百硕自动化环保设备有限公司 | A kind of gas cleaning decoction continuous mixer structure |
| CN107551842B (en) * | 2017-09-28 | 2023-09-01 | 池州市星聚信息技术服务有限公司 | Continuous mixing mechanism for flue gas purification liquid medicine |
| CN108905661A (en) * | 2018-07-27 | 2018-11-30 | 东北石油大学 | A kind of pipe gas liquid mixer and oil field recharged waste water expose oxygen method |
| CN108905661B (en) * | 2018-07-27 | 2021-04-27 | 东北石油大学 | Pipe flow gas-liquid mixer and oil field reinjection sewage oxygen exposure method |
| CN109675476A (en) * | 2018-12-19 | 2019-04-26 | 西安交通大学 | A kind of vertical cluster the bottom of the channel import bubbly two phase flow mixes device and method |
| CN110201589B (en) * | 2019-05-10 | 2020-09-11 | 清华大学 | Micro mixer for dispersing liquid drops or bubbles in high-viscosity fluid |
| CN110201589A (en) * | 2019-05-10 | 2019-09-06 | 清华大学 | A kind of micro-mixer of the dispersant liquid drop in highly viscous fluid or bubble |
| CN110567675A (en) * | 2019-07-24 | 2019-12-13 | 中国空间技术研究院 | Experimental device and method for equivalently implementing gas-liquid distribution in microgravity low-temperature environment |
| CN110567675B (en) * | 2019-07-24 | 2021-06-11 | 中国空间技术研究院 | Experimental device and method for equivalently implementing gas-liquid distribution in microgravity low-temperature environment |
| CN110917924A (en) * | 2019-12-16 | 2020-03-27 | 肖文婷 | Mixing device for chemical foaming |
| CN114831069A (en) * | 2022-05-31 | 2022-08-02 | 福建省寰杰科技发展有限公司 | Seafood culture pond with seawater retreatment device |
| CN114831069B (en) * | 2022-05-31 | 2023-11-28 | 福建省寰杰科技发展有限公司 | Seafood culture pond with sea water reprocessing device |
| CN115350426A (en) * | 2022-08-31 | 2022-11-18 | 徐工消防安全装备有限公司 | Fire-fighting foam foaming device, system and foaming method |
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