CN201239612Y - Static state fluid mixer - Google Patents
Static state fluid mixer Download PDFInfo
- Publication number
- CN201239612Y CN201239612Y CNU2008201207131U CN200820120713U CN201239612Y CN 201239612 Y CN201239612 Y CN 201239612Y CN U2008201207131 U CNU2008201207131 U CN U2008201207131U CN 200820120713 U CN200820120713 U CN 200820120713U CN 201239612 Y CN201239612 Y CN 201239612Y
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Abstract
The utility model relates to a stationary liquid mixer, which comprises a housing and an internal part. The internal part comprises at least two fillers with different types combined in the flow direction. The utility model can be used through collocation of various types of fillers, so as to achieve liquid thorough mixing. Furthermore, the utility model does not need external power, and has the advantages of high mixing efficiency, good mixing effect and low energy consumption, thereby suiting various conditions.
Description
(1) technical field
The utility model relates to a kind of static liquid blender.
(2) background technology
It generally is to adopt to carry out mechanical agitation with the driven by motor paddle in mixer that traditional liquid mixes, and needs consumption of power, and needs the regular hour, and this operation not only can not make medium continuous phase during the course, and mixes inhomogeneously, has influenced reaction speed.
Static mixer is a kind of advanced blender that early seventies begins to develop, U.S. Kai Nisi companies in 1970 release the static mixer of its development first, according to estimates, have at least hundreds of thousands platform static mixer in every field, to use at present in the world, after the eighties, more domestic relevant enterprises also begin to drop into research, have also obtained good application in all fields.Static mixer is different with agitator, and it does not have moving component, is to rely on rational internal element of structure particular design and fluid to flow to realize the mixing of various fluids.Specific energy consumption is low mutually, efficient is high for static mixer and agitator, Venturi tube, orifice plate post, homogenizer etc., reduced investment, volume are little, be easy for serialization production.In static mixer, the rule of " it is overlapping to cut apart a displacement one " is being followed in the motion of fluid, the realization that wherein is shifted for mixed process plays main effect. and displacement mode can be divided into " multichannel is shifted relatively " and " the relative displacement that same cross section velocity flow profile causes " two big classes, and the main displacement mode of different model blender is also different.Static mixer is widely used in industries such as chemical industry, oil, medicine, agricultural chemicals, food, plastics, daily use chemicals, mining and metallurgy, papermaking, chemical fibre, cable, biology, environmental protection.Static mixer not only can be used for mixed process, and can be used for and the relevant process of mixing one transmission, comprises processes such as gas/gas mixing, gas/liquid reactions, liquid/liquid extraction, liquid/liquid reaction and augmentation of heat transfer.Because low, effective, the reduced investment of this product energy consumption, instant effect, institute thinks that the user has obtained considerable economic.
Existing static liquid blender generally includes shell and internals, and internals are generally structured packing.Only contain a kind of filler of model in the existing blender, can only be adapted to the specific occasion, can't satisfy the requirement of various working.
(3) utility model content
Technical problem to be solved in the utility model is to provide a kind of mixing efficiency height, good mixing effect, static liquid blender that energy consumption is low.
Described static liquid blender comprises shell and internals, and described internals are combined along the liquid flow path direction by the filler of different model more than two kinds.
Further, described filler is a plate ripple arranged packing.
Further, described shell is a seamless steel pipe.
Further, described static liquid blender is made up of two sections mixed zone I sections and II section, and the I section is connected through flange with the II section; Described I section and II section contain a kind of filler of different model each other at least respectively.
Further, contain two kinds of fillers of different model each other in the described I section, contain in the II section with the I section in the filler of filler different model.
When the utility model used, by the plate ripple arranged packing of different model, passed through successively by fluid turbulent flow in filler for several blending agents, and the variation that flows to takes place.When fluid passes through filler successively, liquid is divided into thin slice, the power power that its quantity is pressed parts number increases.When thin slice is little during to certain degree, the effect of molecular diffusion is more and more strong, reaches at last to mix.The type selecting of static mixer is to decide according to concrete technological requirement, the structure model that different rerum natura (severe, viscosity, surface tension etc.) requirement adapts with it.Can from the filler of following marque, select to arrange in pairs or groups mutually more than two kinds to obtain desired effects: SM125Y, SM170Y, SM200Y, SM250Y, SM350Y, SM450Y, SM700Y.
The beneficial effects of the utility model are:
1, collocation is used through the filler of multiple model, and liquid reaches abundant mixing, does not need additionaling power, and mixing efficiency height, good mixing effect, energy consumption be low, be adapted to various working;
2, because fluid disturbance in blender is strong, even therefore its wall heat transfer coefficient is also very big in the laminar flow territory;
3, can back-mixing: warp-wise mixes violent, so uniformity of temperature profile, and the existence of filler plate is minimized axial backmixing, and fluid flows and approaches complete piston flow;
4, resistance is very little, Xiao Yu ≦ 5Kpa.
(4) description of drawings
Fig. 1 is the structural representation of embodiment 1 described static liquid blender.
Fig. 2 is the structural representation of embodiment 2 described static liquid blenders.
(5) specific embodiment
The utility model is described in further detail below in conjunction with embodiment, but protection domain of the present utility model is not limited to this.
With reference to Fig. 1, a kind of static liquid blender comprises shell 1 and internals, and described internals are combined along the liquid flow path direction by the filler 2 of different model more than two kinds.
Described filler 2 is a plate ripple arranged packing.
Described shell 1 is a seamless steel pipe.
With reference to Fig. 2, a kind of static liquid blender comprises shell and internals, and described internals are combined along the liquid flow path direction by the filler of different model more than two kinds.
Described static liquid blender is made up of two sections mixed zone I sections 3 and II section 4, and I section 3 is connected through flange 5 with II section 4; Contain two kinds of fillers 6,7 of different model each other in the described I section 3, contain in the II section with the I section in the filler 8 of filler different model.
Described filler 6,7,8 is a plate ripple arranged packing.
Described shell is a seamless steel pipe.
Claims (7)
1, a kind of static liquid blender comprises shell and internals, it is characterized in that: described internals are combined along the liquid flow path direction by the filler of different model more than two kinds.
2, static liquid blender according to claim 1 is characterized in that described filler is a plate ripple arranged packing.
3, static liquid blender according to claim 1 and 2 is characterized in that described shell is a seamless steel pipe.
4, static liquid blender according to claim 1 is characterized in that described static liquid blender is made up of two sections mixed zone I sections and II section, and the I section is connected through flange with the II section; Described I section and II section contain a kind of filler of different model each other at least respectively.
5, static liquid blender according to claim 4 is characterized in that described filler is a plate ripple arranged packing.
6,, it is characterized in that described shell is a seamless steel pipe according to claim 4 or 5 described static liquid blenders.
7, static liquid blender according to claim 4 is characterized in that containing two kinds of fillers of different model each other in the described I section, contain in the II section with the I section in the filler of filler different model.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008201207131U CN201239612Y (en) | 2008-06-30 | 2008-06-30 | Static state fluid mixer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008201207131U CN201239612Y (en) | 2008-06-30 | 2008-06-30 | Static state fluid mixer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201239612Y true CN201239612Y (en) | 2009-05-20 |
Family
ID=40712901
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2008201207131U Expired - Fee Related CN201239612Y (en) | 2008-06-30 | 2008-06-30 | Static state fluid mixer |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201239612Y (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103011100A (en) * | 2012-12-14 | 2013-04-03 | 杭州海虹精细化工有限公司 | Method for synthesizing hydrazine hydrate through high-efficiency mixing by using structured packing |
| CN106925149A (en) * | 2017-04-24 | 2017-07-07 | 苏州纳磐新材料科技有限公司 | Static mixer and mixing arrangement |
| CN109997765A (en) * | 2019-04-10 | 2019-07-12 | 华南农业大学 | A kind of device for continuous-flow type fish exposure test |
-
2008
- 2008-06-30 CN CNU2008201207131U patent/CN201239612Y/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103011100A (en) * | 2012-12-14 | 2013-04-03 | 杭州海虹精细化工有限公司 | Method for synthesizing hydrazine hydrate through high-efficiency mixing by using structured packing |
| CN106925149A (en) * | 2017-04-24 | 2017-07-07 | 苏州纳磐新材料科技有限公司 | Static mixer and mixing arrangement |
| CN106925149B (en) * | 2017-04-24 | 2019-12-10 | 苏州纳磐新材料科技有限公司 | Static mixer and mixing device |
| CN109997765A (en) * | 2019-04-10 | 2019-07-12 | 华南农业大学 | A kind of device for continuous-flow type fish exposure test |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20090520 Termination date: 20170630 |