CN2865838Y - Spray mixing emulsification machine - Google Patents
Spray mixing emulsification machine Download PDFInfo
- Publication number
- CN2865838Y CN2865838Y CN 200620039272 CN200620039272U CN2865838Y CN 2865838 Y CN2865838 Y CN 2865838Y CN 200620039272 CN200620039272 CN 200620039272 CN 200620039272 U CN200620039272 U CN 200620039272U CN 2865838 Y CN2865838 Y CN 2865838Y
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- mixing
- spraying
- mixing kettle
- guide plate
- emulsifier
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Abstract
A spraying mixing emulsator comprising mixing kettle, feed tank, atomization device, residual oil pump, resistance thermometer sensor temperature probe, three-way valve and feed filter pipe. Spraying channel and guide bar are set in spraying device. Turbulent flux is set in spraying channel and fluid running is in turbulent status. Molecule striking and friction fluid material will occur in turbulent channel for mixing fluid material and thinning granule. Fluid material can spray fogged emulsion in even and fine granule. Moreover, with the setup of guide bar, the fluid material can form small scope fleeing. Therefore, the mixing and emulsification effect will be better. The latex produced will not delaminate and deposit and the storage life can be over two years. The utility model spraying mixing emulsator is a kind of simple equipment with low cost, energy consumption, fine emulsification, economic and practical performances. It is not only suitable for fuel emulsification and also can be used for emulsion extraction in foods and medicine fields, etc.
Description
Technical field
The utility model relates to the spraying Mixingemulsificationmachine that two or more liquid medium mixes mutually.
Background technology
As everyone knows, two kinds of liquid mediums of different liquid phases mix under certain external force positive action, can form a kind of uniform state mixed liquor.This mixed liquor can keep certain resting period under static condition, generally, the resting period of mixed liquor is except outside the Pass having with the emulsifying agent that adds, and also the equipment with the emulsion process employing has substantial connection.Existing various emulsifier has different operation principles, traditional mechanical agitation type that can be, and injecting type, the ultrasonic vibration formula, magnetic-types etc. all are difficult to make mixed liquor to reach desirable emulsifying effectiveness.More novel centrifugal high-speed cutting formula emulsifier is also because of the equipment complexity, and cost is expensive, high energy consumption, and efficient is low, is difficult to wide popularization and application in medium-sized and small enterprises.
In recent years, because global petroleum resources shortage impels various countries that the research and development of new forms of energy are more and more paid attention to.Especially to the research of fuel emulsification, reaching the fuel oil modification, purposes such as energy-conservation and environmental protection, substantial contribution is all dropped in countries in the world, and to attempt making a kind of equipment simple, and cost is low, and energy consumption is low, and the mulser that efficient is high is to satisfy the needs in market.
Summary of the invention
The utility model provides a kind of spraying mixing emulsifier, and it is that a kind of equipment is simple, and cost is low, and energy consumption is low, emulsify well, and economical and practical emulsifier product is not only applicable to the emulsification of fuel oil, is applicable to food yet, uses during medicine and other are industrial.
The structure of the utility model spraying mixing emulsifier mainly comprises mixing kettle, head tank, sprayer unit, residual oil pump, thermal resistance temperature measuring head, three-way valve and drainage conduit.The charge pipe of described head tank bottom be installed in mixing kettle on cover, and stretch in the mixing kettle.Described sprayer unit comprises spray channel and guide plate.Spray channel comprises the nozzle entrance that communicates successively, turbulent flow road, hybrid chamber and jet expansion.Nozzle entrance is infundibulate, and the diameter in turbulent flow road is 1.2-3mm, and two sides of hybrid chamber wall respectively are provided with a liquid conductance mouth.Guide plate is vertically to being arranged on the spray channel, and between liquid conductance mouth and jet expansion, is covered with aperture on the guide plate, and the aperture of aperture is 1-3mm, and the percent opening on the guide plate is 60-80%.Also a screen pack can be set below mixing kettle.Described residual oil pump places on the connecting pipe between three-way valve and the mixing kettle bottom discharge mouth, and drainage conduit links to each other with three-way valve.Described thermal resistance temperature measuring head is fixedly set in the mixing kettle, and the loam cake that passes mixing kettle by lead links to each other with the temperature indicator.
The design feature of the spraying mixing emulsifier that the utility model provides is to be provided with spray channel and guide plate in sprayer unit, be provided with the turbulent flow road in the spray channel, the reynolds number Re (ratio of inertia force during liquid flow and internal friction is called Reynolds number) of liquid stream is greater than 3000, therefore liquid stream is turbulent flow, molecules strike and friction take place in the liquid material in the turbulent flow road, the liquid material is mixed and more refinement of particle, and the liquid material goes out the turbulent flow road sprays vaporific emulsion from even fine particle to hybrid chamber.Again because the setting of guide plate, thereby make the inside and outside pressure differential that produces of hybrid chamber wall, the liquid material is fled among a small circle by liquid conductance interruption-forming again, make the mixing and emulsifying effect better.The mixed emulsion of producing, not stratified, do not precipitate, storage life was more than 2 years.Reaction temperature can raise automatically gradually in whole circulation spraying mixing and emulsifying process, must not use heater more in addition, saves the energy.
Therefore the utility model is that a kind of equipment is simple, and cost is low, and energy consumption is low, emulsify well, and economical and practical emulsifier product, the utility model is not only applicable to the emulsification of fuel oil, is applicable to that production fields such as food, medicine produce emulsion yet.
Description of drawings
Fig. 1 is the structural representation of the utility model spraying mixing emulsifier.
Fig. 2 is the longitudinal sectional drawing of sprayer unit among Fig. 1.
Fig. 3 is the left view of guide plate among Fig. 2.
The specific embodiment
The spraying mixing emulsifier of the utility model design, its structure mainly comprises mixing kettle 3 as shown in Figure 1-Figure 3, head tank 6, sprayer unit 5, residual oil pump 1, thermal resistance temperature measuring head 2, three-way valve 7 and drainage conduit 4.The charge pipe 9 of described head tank 6 bottoms be installed in mixing kettle 3 on cover, and stretch in the mixing kettle 3.Described sprayer unit 5 comprises spray channel 19 and guide plate 15.Spray channel 19 comprises the nozzle entrance 10 that communicates successively, turbulent flow road 11, hybrid chamber 12 and jet expansion 13.Nozzle entrance 10 is infundibulate, and the diameter in turbulent flow road 11 is 1.2-3mm.Two sides of hybrid chamber 12 walls respectively are provided with a liquid conductance mouth 14.Guide plate 15 is vertically to being arranged on the spray channel 19, and between liquid conductance mouth 14 and jet expansion 13, is covered with aperture 16 on the guide plate 15, and the aperture of aperture 16 is 1-3mm, and the percent opening on the guide plate 15 is 60-80%.Also a screen pack 20 can be set below mixing kettle 3, to remove impurity.Described residual oil pump 1 places on the connecting pipe 8 between three-way valve 7 and the mixing kettle 3 bottom discharge mouths 18, and residual oil pump 1 is used for the liquid material of delivery cycle spraying mixing and emulsifying, even the advantage of residual oil pump 1 is some little bits in the liquid material, does not also influence the running of pump.Drainage conduit 4 links to each other with three-way valve 7.Described thermal resistance temperature measuring head 2 is fixedly set in the mixing kettle 3, and the loam cake that passes mixing kettle 3 by lead links to each other with temperature indicator 17, to show the mixed liquor material situation that temperature rises in circulation mixed atomizing emulsion process.
The operation principle of the spraying Mixingemulsificationmachine of the utility model design is as follows: material liquid for example fuel oil and emulsifying agent etc. enters in the mixing kettle 3 by head tank 6 and charge pipe 9 thereof, the three-way valve 7 and the passage of nozzle entrance 10 are opened, and close passage with drainage conduit 4, start residual oil pump 1, the mixed liquor material that is flowed out by mixing kettle 3 bottom discharge mouths 18 by screen pack 20 is through residual oil pump 1, pipeline 8 and three-way valve 7 enter the nozzle entrance 10 of sprayer unit 5, enter turbulent flow road 11, liquid flow is the turbulent flow attitude, therefore molecules strike and friction take place in liquid stream in turbulent flow road 11, the liquid material is mixed and more refinement of particle, and the liquid material goes out the vaporific emulsion of turbulent flow road 11 to the even fine particle of hybrid chamber 12 ejections.And go out at a high speed by jet expansion 13, the anti-phase aperture 16 that passes on the guide plate 15 of part liquid material enters outside hybrid chamber 12 walls, thereby make the inside and outside generation pressure differential of hybrid chamber 12 walls, the liquid material is formed by liquid conductance mouth 14 again flee among a small circle, make the mixing and emulsifying better effects if.Make the mixed liquor material by mixing kettle 3 bottom discharge mouths 18 like this, residual oil pump 1 constitutes a closed circuit with sprayer unit 5, in the mixing and emulsifying process is sprayed in circulation repeatedly, temperature in the mixing kettle 3 rises gradually, measure by thermal resistance temperature measuring head 2, on temperature indicator 17, demonstrate the situation of temperature, after the feed liquid of mixing is finished mixing and emulsifying, with closing all of three-way valve 7 and nozzle entrance 10, and open passage with drainage conduit 4, mix the fuel emulsification liquid that the back forms and discharge from drainage conduit 4.
Claims (3)
- One kind the spraying mixing emulsifier, the structure that it is characterized in that this emulsifier mainly comprises mixing kettle (3), head tank (6), sprayer unit (5), residual oil pump (1), thermal resistance temperature measuring head (2), three-way valve (7) and drainage conduit (4), the charge pipe (9) of described head tank (6) bottom be installed in mixing kettle (3) on cover, and stretch in the mixing kettle (3); Described sprayer unit (5) comprises spray channel (19) and guide plate (15), spray channel (19) comprises the nozzle entrance (10) that communicates successively, turbulent flow road (11), hybrid chamber (12) and jet expansion (13), nozzle entrance (10) is infundibulate, the diameter in turbulent flow road (11) is 1.2-3mm, the both sides of hybrid chamber (12) wall respectively are provided with a liquid conductance mouth (14), guide plate (15) is vertically to being arranged on the spray channel (19), and be positioned between liquid conductance mouth (14) and the jet expansion (13), be covered with aperture (16) on the guide plate (15); Described residual oil pump (1) places on the connecting pipe (8) between three-way valve (7) and mixing kettle (3) the bottom discharge mouth (18), and drainage conduit (4) links to each other with three-way valve (7); Described thermal resistance temperature measuring head (2) is fixedly set in the mixing kettle (3), and the loam cake that passes mixing kettle (3) by lead links to each other with temperature indicator (17).
- 2. spraying mixing emulsifier as claimed in claim 1 is characterized in that the aperture of the aperture (16) that is covered with on the described guide plate (15) is 1-3mm, and the percent opening on the guide plate (5) is 60-80%.
- 3. spraying mixing emulsifier as claimed in claim 1 is characterized in that in the below of mixing kettle (3) screen pack (20) being set.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200620039272 CN2865838Y (en) | 2006-01-26 | 2006-01-26 | Spray mixing emulsification machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200620039272 CN2865838Y (en) | 2006-01-26 | 2006-01-26 | Spray mixing emulsification machine |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2865838Y true CN2865838Y (en) | 2007-02-07 |
Family
ID=37701538
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200620039272 Expired - Fee Related CN2865838Y (en) | 2006-01-26 | 2006-01-26 | Spray mixing emulsification machine |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2865838Y (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102718612A (en) * | 2012-07-03 | 2012-10-10 | 山西惠丰特种汽车有限公司 | Static mixer for emulsion |
| CN103070937A (en) * | 2013-01-21 | 2013-05-01 | 蒋清校 | Preparation method of peony essential oil for beriberi |
| CN111957219A (en) * | 2019-09-02 | 2020-11-20 | 陈捷 | Preparation device and method of emulsified water and emulsified diesel oil |
| TWI787208B (en) * | 2016-09-30 | 2022-12-21 | 南韓商愛茉莉太平洋股份有限公司 | Apparatus for preparing cosmetic composition containing thickener added to emulsion substance formed by instant emulsification using microfluidic channel |
-
2006
- 2006-01-26 CN CN 200620039272 patent/CN2865838Y/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102718612A (en) * | 2012-07-03 | 2012-10-10 | 山西惠丰特种汽车有限公司 | Static mixer for emulsion |
| CN103070937A (en) * | 2013-01-21 | 2013-05-01 | 蒋清校 | Preparation method of peony essential oil for beriberi |
| CN103070937B (en) * | 2013-01-21 | 2014-11-05 | 慈溪市校杰电器有限公司 | Preparation method of peony essential oil for beriberi |
| TWI787208B (en) * | 2016-09-30 | 2022-12-21 | 南韓商愛茉莉太平洋股份有限公司 | Apparatus for preparing cosmetic composition containing thickener added to emulsion substance formed by instant emulsification using microfluidic channel |
| CN111957219A (en) * | 2019-09-02 | 2020-11-20 | 陈捷 | Preparation device and method of emulsified water and emulsified diesel oil |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20070207 Termination date: 20100228 |