CN203750478U - Micro-channel oil-water mixing device - Google Patents
Micro-channel oil-water mixing device Download PDFInfo
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- CN203750478U CN203750478U CN201420151162.0U CN201420151162U CN203750478U CN 203750478 U CN203750478 U CN 203750478U CN 201420151162 U CN201420151162 U CN 201420151162U CN 203750478 U CN203750478 U CN 203750478U
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- oil
- microchannel
- coil pipe
- water
- tubular type
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Abstract
The utility model discloses a micro-channel oil-water mixing device. The micro-channel oil-water mixing device comprises a tubular premixer and a micro-channel coil pipe, wherein one end of the tubular premixer is provided with an oil inlet and a water inlet, and the other end of the tubular premixer is connected with the micro-channel coil pipe; the tubular premixer is internally provided with a stainless steel screen which is coiled to be cylindrical. The micro-channel oil-water mixing device disclosed by the utility model has the advantages of simple structure, convenience in using and high oil-water mixing efficiency.
Description
Technical field
The utility model relates to a kind of mixing arrangement, relates in particular to a kind of microchannel oil-water mixer.
Background technology
In polymerization technique, need water and other oily matter to mix, form the mixture mixing, mixture can be produced high-quality resin particle uniformly, so require very high to the mixed effect of oil-water mixer.The hybrid mode of oil and water has two kinds at present: the one, oil is added to the water, and realize mixing by stirring; The 2nd, together with by Venturi tube, oil being blended directly in water.Although above-mentioned two kinds of modes are simple, all can not realize the abundant mixing of oil and water.
China Patent Publication No. CN202410539A discloses a kind of two oil-water mixer, be used for making pitch to be dispersed in emulsion, comprise mixing arrangement, bitumen feed device and emulsion feed arrangement, described bitumen feed device and emulsion feed arrangement all pass into described mixing arrangement inside, the pitch outlet of described bitumen feed device can make pitch dilution fully in emulsion disperse higher than the emulsion outlet of described emulsion feed arrangement, improve the quality of emulsified asphalt, and reduced the destruction to mixing apparatus.
China Patent Publication No. CN203002233A discloses a kind of oil mixing with water static mixer, it comprises: a pipe fitting, it in axial direction has input and an output of an input water, described pipe fitting is also connected with an oil inlet pipe conducting, described oil inlet pipe has an oil-out, and this oil-out is positioned at pipe fitting; At least two baffle plates, are located in pipe fitting along the axial direction of described pipe fitting, have a spacing between each baffle plate, and on described each baffle plate, are equipped with densely covered and equally distributed through hole.
China Patent Publication No. CN103084123A discloses a kind of fluid by one or more holes method, system and equipment that this fluid is mixed with one other fluid in the time flowing through a microchannel.The method comprises: the first reactant is flowed in microchannel; Microchannel is limited by one or more microchannel wall, has at least one hole in the wall of microchannel; The Part I of microchannel is limited by the first hydraulic diameter, and Part II is limited by the second hydraulic diameter of the hydraulic diameter that is greater than Part I; Part I is arranged on the upstream of Part II; At least one hole is arranged on the upstream of Part II; Make the second reactant at least one hole of flowing through enter microchannel.This device more complicated.
Existing document and patented technology all can not realize the abundant mixing of oil and water, or hybrid technique is comparatively complicated.
Summary of the invention
The purpose of this utility model is the defect that overcomes prior art, and a kind of simple in structure, easy to use, microchannel oil-water mixer that mixing efficiency is high is provided.
For solving the problems of the technologies described above, the technical solution adopted in the utility model is as follows: a kind of microchannel oil-water mixer, comprise tubular type premixer and microchannel coil pipe, described tubular type premixer one end is provided with oil-in and water inlet, the other end is connected with described microchannel coil pipe, in described tubular type premixer, is provided with and is rolled into stainless steel cloth cylindraceous.
The coil pipe internal diameter of described microchannel coil pipe is preferably 0.5-2mm.
The shape of described microchannel coil pipe is preferably spring-like spirality.
The screw diameter of described microchannel coil pipe (2) is preferably 20-30mm.
The specification of described stainless steel cloth is preferably order.
The microcosmic that the utility model has been realized profit mixes, and it is the mixing on molecular scale that microcosmic mixes, and it has important impact to fast reaction processes such as burning, polymerization, organic synthesis, precipitation, crystallizations.Its reason be Quickly react system need short time of staying and high-intensity local mixing with avoid on molecular scale from collection.Microchannel of the present utility model oil-water mixer, has solved traditional poor technical problem of oil mixing with water complex process, mixed effect, have advantages of simple in structure, easy to use, mixing efficiency is high.
Compared with prior art, the utility model has the advantage of:
1, mixing efficiency is high, the utility model realized profit microcosmic mix, avoid on molecular scale from collection, make profit obtain abundant mixing; The existing higher mixed effect of this mixing arrangement, maneuverable advantage.
2, simple in structure, easy to operate, the utility model is simple in structure, easy to operate, can be widely used in the oil mixing with water operation in polymerization technique.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model.
In figure, tubular type premixer 1, microchannel coil pipe 2, stainless steel cloth 3, oil-in 4, water inlet 5.
Detailed description of the invention
Structure of the present utility model is referring to Fig. 1, a kind of microchannel oil-water mixer, comprise tubular type premixer 1 and microchannel coil pipe 2, tubular type premixer 1 one end is provided with oil-in 4 and water inlet 5, the other end is connected with described microchannel coil pipe 2, is provided with and is rolled into stainless steel cloth 3 cylindraceous in described tubular type premixer 1.
Workflow of the present utility model is: oil is inputted tubular type premixer 1 from oil-in 4, water is inputted tubular type premixer 1 from water inlet 5, liquid is flowed after dissection premixed through being rolled into stainless steel cloth 3 cylindraceous in tubular type premixer 1, further mix through microchannel coil pipe 2, the oil water mixture mixing flows out from 2 outlets of microchannel coil pipe again.
Below in conjunction with drawings and Examples, the utility model is explained in further detail, but the utility model is not limited in described embodiment.
Embodiment 1
A kind of microchannel oil-water mixer, comprise tubular type premixer 1 (specification: diameter 32mm, length is 1000mm; Material is carbon steel) and the spiral microchannel of spring-like coil pipe 2 (coil pipe internal diameter 0.5mm, screw diameter is 30mm, length is 10m, material is stainless steel), tubular type premixer 1 one end is provided with oil-in 4 (diameter 8mm) and water inlet 5 (diameter 6mm), the other end is connected with microchannel coil pipe 2, is provided with and is rolled into stainless steel cloth 3 cylindraceous (specification: 100 orders) in tubular type premixer 1.
Kerosene is inputted to tubular type premixer 1 from oil-in 4, and water is inputted tubular type premixer 1 from water inlet 5, after 1 premixed of tubular type premixer, more further mixes through microchannel coil pipe 2, and the oil water mixture mixing flows out from 2 outlets of microchannel coil pipe.It is even that oil-water emulsion is observed in sampling, without lamination.
Embodiment 2
A kind of microchannel oil-water mixer, comprise tubular type premixer 1 (specification: diameter 25mm, length is 100mm; Material is carbon steel) and the spiral microchannel of spring-like coil pipe 2 (coil pipe internal diameter 1mm, screw diameter is 20mm, length is 15m, material is stainless steel), tubular type premixer 1 one end is provided with oil-in 4 (diameter 6mm) and water inlet 5 (diameter 10mm), the other end is connected with microchannel coil pipe 2, is provided with and is rolled into stainless steel cloth 3 cylindraceous (specification: 80 orders) in tubular type premixer 1.
Diesel oil is inputted to tubular type premixer 1 from oil-in 4, and water is inputted tubular type premixer 1 from water inlet 5, after 1 premixed of tubular type premixer, more further mixes through microchannel coil pipe 2, and the oil water mixture mixing flows out from 2 outlets of microchannel coil pipe.It is even that oil-water emulsion is observed in sampling, without lamination.
Embodiment 3
A kind of microchannel oil-water mixer, comprise tubular type premixer 1 (specification: diameter 50mm, length is 2000mm; Material is carbon steel) and the spiral microchannel of spring-like coil pipe 2 (coil pipe internal diameter 2mm, screw diameter is 25mm, length is 30m, material is stainless steel), tubular type premixer 1 one end is provided with oil-in 4 (diameter 10mm) and water inlet 5 (diameter 15mm), the other end is connected with microchannel coil pipe 2, is provided with and is rolled into stainless steel cloth 3 cylindraceous (specification: 60 orders) in tubular type premixer 1.
Solvent naphtha is inputted to tubular type premixer 1 from oil-in 4, and water is inputted tubular type premixer 1 from water inlet 5, after 1 premixed of tubular type premixer, more further mixes through microchannel coil pipe 2, and the oil water mixture mixing flows out from 2 outlets of microchannel coil pipe.It is even that oil-water emulsion is observed in sampling, without lamination.
Stainless steel cloth packing method of the present utility model: will be rolled into columned stainless steel cloth and tie up, plug is in tubular type premixer, in sealing tubular type premixer.Change for convenience stainless steel cloth, tubular type premixer one end can be sealed, the other end is designed to the capping that can open, and stainless steel cloth is tied up after spooling, and fills in tubular type premixer 1, then capping is closed.
Claims (5)
1. a microchannel oil-water mixer, comprise tubular type premixer (1) and microchannel coil pipe (2), it is characterized in that, described tubular type premixer (1) one end is provided with oil-in (4) and water inlet (5), the other end is connected with described microchannel coil pipe (2), in described tubular type premixer (1), is provided with and is rolled into stainless steel cloth cylindraceous (3).
2. microchannel according to claim 1 oil-water mixer, is characterized in that the coil pipe internal diameter of described microchannel coil pipe (2) is 0.5-2mm.
3. microchannel according to claim 1 oil-water mixer, what it is characterized in that described microchannel coil pipe (2) is shaped as spring-like spirality.
4. microchannel according to claim 3 oil-water mixer, is characterized in that the screw diameter of described microchannel coil pipe (2) is 20-30mm.
5. microchannel according to claim 1 oil-water mixer, is characterized in that the specification of described stainless steel cloth (3) is order.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201420151162.0U CN203750478U (en) | 2014-03-27 | 2014-03-27 | Micro-channel oil-water mixing device |
Applications Claiming Priority (1)
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CN201420151162.0U CN203750478U (en) | 2014-03-27 | 2014-03-27 | Micro-channel oil-water mixing device |
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CN201420151162.0U Expired - Fee Related CN203750478U (en) | 2014-03-27 | 2014-03-27 | Micro-channel oil-water mixing device |
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Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106582458A (en) * | 2015-10-16 | 2017-04-26 | 世能华奇(北京)科技发展有限公司 | Manufacturing method of mixed diesel, mixed diesel manufactured through method and manufacturing device |
CN109133297A (en) * | 2017-12-05 | 2019-01-04 | 广州市地龙环保技术有限公司 | A kind of precipitation reaction pond |
CN112108283A (en) * | 2020-09-08 | 2020-12-22 | 杭州浙大天元科技有限公司 | High-viscosity waste liquid emulsification and atomization integrated spray gun and high-viscosity waste liquid atomization method |
CN114425286A (en) * | 2020-10-29 | 2022-05-03 | 中国石油化工股份有限公司 | Olefin hydration reaction system and olefin hydration method |
WO2022089530A1 (en) * | 2020-10-28 | 2022-05-05 | 中国石油化工股份有限公司 | Liquid-liquid mixer, liquid-liquid reaction apparatus comprising liquid-liquid mixer, and liquid-liquid reaction method using liquid-liquid mixer |
-
2014
- 2014-03-27 CN CN201420151162.0U patent/CN203750478U/en not_active Expired - Fee Related
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106582458A (en) * | 2015-10-16 | 2017-04-26 | 世能华奇(北京)科技发展有限公司 | Manufacturing method of mixed diesel, mixed diesel manufactured through method and manufacturing device |
CN109133297A (en) * | 2017-12-05 | 2019-01-04 | 广州市地龙环保技术有限公司 | A kind of precipitation reaction pond |
CN112108283A (en) * | 2020-09-08 | 2020-12-22 | 杭州浙大天元科技有限公司 | High-viscosity waste liquid emulsification and atomization integrated spray gun and high-viscosity waste liquid atomization method |
WO2022089530A1 (en) * | 2020-10-28 | 2022-05-05 | 中国石油化工股份有限公司 | Liquid-liquid mixer, liquid-liquid reaction apparatus comprising liquid-liquid mixer, and liquid-liquid reaction method using liquid-liquid mixer |
CN114505017A (en) * | 2020-10-28 | 2022-05-17 | 中国石油化工股份有限公司 | Olefin hydration reaction device and olefin hydration method |
CN114505017B (en) * | 2020-10-28 | 2022-11-11 | 中国石油化工股份有限公司 | Olefin hydration reaction device and olefin hydration method |
CN114425286A (en) * | 2020-10-29 | 2022-05-03 | 中国石油化工股份有限公司 | Olefin hydration reaction system and olefin hydration method |
CN114425286B (en) * | 2020-10-29 | 2023-10-10 | 中国石油化工股份有限公司 | Olefin hydration reaction system and olefin hydration method |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140806 Termination date: 20170327 |
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CF01 | Termination of patent right due to non-payment of annual fee |