CN1958139A - High-pressure homogeneous device - Google Patents
High-pressure homogeneous device Download PDFInfo
- Publication number
- CN1958139A CN1958139A CN 200510117345 CN200510117345A CN1958139A CN 1958139 A CN1958139 A CN 1958139A CN 200510117345 CN200510117345 CN 200510117345 CN 200510117345 A CN200510117345 A CN 200510117345A CN 1958139 A CN1958139 A CN 1958139A
- Authority
- CN
- China
- Prior art keywords
- unit
- inner face
- pressure homogeneous
- homogeneous device
- flow
- 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
- 241001672694 Citrus reticulata Species 0.000 claims description 19
- 230000008676 import Effects 0.000 claims description 3
- 239000007788 liquid Substances 0.000 description 8
- 238000007599 discharging Methods 0.000 description 4
- 230000000712 assembly Effects 0.000 description 3
- 238000000429 assembly Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 230000008901 benefit Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000009795 derivation Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000004945 emulsification Methods 0.000 description 1
- 239000003995 emulsifying agent Substances 0.000 description 1
- 239000000839 emulsion Substances 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 230000003116 impacting effect Effects 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000003801 milling Methods 0.000 description 1
- 235000019476 oil-water mixture Nutrition 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 239000012071 phase Substances 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000010008 shearing Methods 0.000 description 1
Images
Abstract
A high-pressure homogenizing mechanism has a leading-in module with the first internal end face and the first external end face, at least two flow-in units arranged at the predefined positions of said leading-in module and with an inlet hole between said internal and external end faces and a guide slot on said internal end face, a leading-out module with the second internal end face and the second external end face, and at least one flow-out unit between said second internal and external end faces and communicated with the predefined position of said flow-in unit.
Description
Technical field
The present invention relates to high-pressure homogeneous device, be meant a kind of runner especially, with the Flow guiding structure of the high-pressure homogeneous device of promoting its applicability and usefulness with diversified relative angle.
Background technology
The following alleged high-pressure homogeneous device (High Pressure Homogenizer) of the present invention, refer to utilize high pressure group Pu that mixing material is forced into specified pressure, and this mixing material is delivered to a homogenizing valve (Homogenizing Valve) with a pressure duct, again by the long-pending reduction design of the cross section of fluid channel that this homogenizing valve had, original high pressure mixing liquid is converted to high-speed mixing liquid (its stream scooter 600m/s), utilize two strands of high-speed mixing liquid when crossing, the impulsive force that is produced, shearing force, effect such as air pocket and step-down is to carry out the powder grinding dispersion, application such as oil-water mixture emulsification or clasmatosis.
Compare with traditional milling apparatus, high-pressure homogeneous device is owing to rarer pollutant in the process produces, and process time is short, therefore becomes the industry main flow equipment of employing in a large number gradually.
Just known in the art, the U.S. the 4th, 533, No. 254 a kind of devices that utilize high-pressure homogeneous device (High Pressure Homogenizer) to make emulsion of patent disclosure, be to insert and put a distance piece between a pan feeding microscope carrier and a discharging microscope carrier, and in respectively going into, form a runner between discharging microscope carrier and the distance piece, the pan feeding microscope carrier has two of being connected to the runner two ends and goes into discharge orifice, in order to input high pressure mixing liquid, the discharging microscope carrier has a relief port that is connected in these runner central authorities; So that two strands of high pressure mixing liquid impact in opposite directions at the runner central part, and after finishing reaction, discharge by relief port more by this.
Other has a kind of emulsifier unit of a Japanese JP2261525 patent disclosure, be on a pan feeding microscope carrier, to be provided with two to go into discharge orifice and be communicated to one end respectively, and give connection by a straight trough of being located on this end face, two relief port are set on another discharging microscope carrier are communicated to one end respectively, and give connection by a translot of being located on this end face, during operation, with biend combination in opposite directions, and make each straight trough intersect and be communicated with the central part of translot, make by this and enter this two high pressure mixing liquid of going in the discharge orifice, can impact in opposite directions at the straight trough central part, and after finishing reaction, be directed to this two relief port via translot and discharge.
The disclosed technology of this Japan Patent, no doubt with the disclosed three-piece construction of above-mentioned United States Patent (USP), be improved as two formulas being convenient to process and make up, but on making its must be respectively respectively become a mandarin microscope carrier with go out to flow on the microscope carrier, each straight trough and translot are manufactured in processing respectively, and it is constant in order to guide the mutual direction of impacting of high pressure mixing liquid phase, and is not suitable for and need impacts and the occasion of reacting with different angles.
Summary of the invention
For solving above-described problems of the prior art, main purpose of the present invention promptly is to provide a kind of Flow guiding structure of high-pressure homogeneous device, and it has is convenient to change the runner direction to promote the effect of result of use.
Another object of the present invention is to provide a kind of Flow guiding structure of high-pressure homogeneous device, it has the advantage of conveniently manufacturing runner.
For reaching aforesaid purpose, the present invention discloses a kind of Flow guiding structure of high-pressure homogeneous device, includes: one imports assembly, has one first inner face and one first outer face; The predetermined position of this importing assembly is located at least two unit that become a mandarin; The unit that respectively becomes a mandarin has discharge orifice respectively and is communicated between each first inner face and first outer face, and one guiding gutter be located on first inner face, the one end is gone into discharge orifice and is communicated with corresponding, and the other end then extends and is connected with the guiding gutter of another unit that becomes a mandarin towards predetermined direction; One derives assembly, has one second inner face and one second outer face with the first inner face butt; At least onely go out to flow the unit, be communicated between second inner face and second outer face, and be connected with the predetermined position of the unit that becomes a mandarin.
Description of drawings
Fig. 1 is the allocation plan of preferred embodiment of the present invention () user mode.
Fig. 2 is preferred embodiment of the present invention (one's) a schematic perspective view.
Fig. 3 is preferred embodiment of the present invention (twos') a schematic perspective view.
Fig. 4 is preferred embodiment of the present invention (threes') a schematic perspective view.
Fig. 5 is preferred embodiment of the present invention (fours') a schematic perspective view.
Fig. 6 is the front view of its importing assembly of preferred embodiment of the present invention (four).
Fig. 7 is the front view of its importing assembly of preferred embodiment of the present invention (five).
Fig. 8 is preferred embodiment of the present invention (sixs') a schematic perspective view.
Fig. 9 is preferred embodiment of the present invention (sevens') a schematic perspective view.
Wherein, Reference numeral:
10 Flow guiding structures, 11 positioning components
20 import assembly 12 sleeve pipes
22 first inner faces, 13 connectors
24 first outer faces, 14 latch assemblies
Assemblies are derived in 26,28 become a mandarin unit 30
260,280 go into discharge orifice 32 second inner faces
262,282 guiding gutters, 34 second outer faces
264,284 splitter boxs 36 go out to flow the unit
The specific embodiment
For said structure of the present invention, feature and effect can be become apparent, lift some preferred embodiments now, and cooperate appended graphicly, further be described in detail as follows.
At first see also Fig. 1,2, Flow guiding structure 10 disclosed in this invention is derived 30 of assemblies by the importing assembly 20 and that can combine closely in opposite directions and is formed jointly.Be placed in during use among the tubulose positioning component 11, its two ends are respectively a sleeve pipe 12 and prop up with a connection piece 13, and the two ends of this positioning component 11 respectively are provided with a latch assembly 14 again, in order to by two ends each sleeve pipe 12 and connector 13 of packing in opposite directions.
Importing assembly 20 has: one first inner face 22 and one first outer face 24, and the central part of this importing assembly 20 is located at least two unit that become a mandarin (26,28); Unit (26 respectively becomes a mandarin, 28) include respectively again into discharge orifice (260,280) be communicated between each first inner face 22 and first outer face 24, an and guiding gutter (262,282) be arranged with on first inner face 22, one end of a guiding gutter 262 is wherein gone into discharge orifice 260 and is communicated with corresponding, the other end then along a straight line direction extend (being as the criterion) down and be connected with another guiding gutter 282 upper ends of extending along same rectilinear direction with the accompanying drawing direction.
Each first, second inner face (22,32) combine closely in opposite directions after, can be for the high pressure mixing liquid (not shown) outside first inner face 22, respectively via respectively going into discharge orifice (260,280) flow to corresponding each guiding gutter (262,282), and impact in opposite directions to react in its river outlet, make the mixed liquor through reacting again, drain into outside second outer face 34 via going out to flow unit 36.
Importing assembly 20 shown in Fig. 3 be that become a mandarin each guiding gutter (262,282) on the unit (26,28) of set this on it two is arranged to separately along a straight line direction and extends, and this two rectilinear direction is vertical mutually.
Importing assembly 20 shown in Fig. 4 which is provided with and makes its guiding gutter 262 be one on the other a pair of unit 26 that becomes a mandarin that extends in opposite directions, and makes its guiding gutter 282 be a pair of unit 28 that becomes a mandarin of the right horizontal expansion of a first from left; Derive and to go out to flow unit 36 on the assembly 30, extend to an end of second inner face 32, then with longitudinal extension to guiding gutter 262, and the river outlet correspondence to guiding gutter 282 of horizontal expansion.
Each guiding gutter (262 shown in the earlier figures 2,3,4,282), no doubt can be made as respectively and extend along overlapping or orthogonal two rectilinear directions, but in the utilization of reality, the angle that bearing of trend defined jointly of this two straight line, the high pressure mixing liquid of flowing through therebetween can be made as between 5 ° to 180 °, so that can different angles impact and reaction.
The unit that respectively becomes a mandarin (26,28) shown in Fig. 5,6, above-mentioned each guiding gutter (262,282) are made as respectively and extend along a direction of a curve, and this two terminal phase joining place is extended along same tangential direction t.
The unit (26 that respectively becomes a mandarin shown in Figure 7,28), has forniciform guiding gutter (262,282) equally respectively, each guiding gutter (262,282) end that is connected mutually, (t1 t2) extends along a tangent line direction respectively, this two tangential direction (t1, t2) not only be parallel to each other and be separated by one suitably to d, this is apart from d half less than each guiding gutter (262,282) width.
The importing assembly 20 of the Flow guiding structure 10 shown in Fig. 8,9, further be concaved with two splitter boxs (264 on its first inner face 22,284), each splitter box (264,284) has suitable length respectively, and with one end and each guiding gutter (262,282) intersection area is connected, and in the present embodiment, its other end is respectively along each corresponding splitter box (262,282) bearing of trend continues to extend a suitable length again; Then be provided with two on the derivation assembly 30 and go out to flow unit 36, extend to an end and the terminal connection of each splitter box (264,284) of this second inner face 32 respectively with it.Use to make and impact and reaction mixed liquor later, respectively go out to flow unit 36 with corresponding, flow to this second outer face 34 via each splitter box (264,284).
Claims (8)
1. the Flow guiding structure of a high-pressure homogeneous device is characterized in that, includes:
One imports assembly, has one first inner face and one first outer face; The predetermined position of described importing assembly is located at least two unit that become a mandarin; The unit that respectively becomes a mandarin has discharge orifice respectively and is communicated between each first inner face and first outer face, and one guiding gutter be located on described first inner face, the one end is gone into discharge orifice and is communicated with corresponding, and the other end then extends and is connected with the guiding gutter of another unit that becomes a mandarin towards predetermined direction; And
One derives assembly, has one second inner face and one second outer face with the described first inner face butt; At least onely go out to flow the unit, be communicated between described second inner face and second outer face, and be connected with the predetermined position of the described unit that becomes a mandarin.
2. according to the Flow guiding structure of the described high-pressure homogeneous device of claim 1, it is characterized in that described two guiding gutters extend along same rectilinear direction.
3. according to the Flow guiding structure of the described high-pressure homogeneous device of claim 1, it is characterized in that, described two guiding gutters respectively along a straight line direction extend, this two straight line be parallel to each other and standoff distance less than half of each guiding gutter width.
4. according to the Flow guiding structure of the described high-pressure homogeneous device of claim 1, it is characterized in that, described two guiding gutters respectively along a straight line direction extend, and this two straight line defines a angle between 5 ° to 180 ° jointly.
5. according to the Flow guiding structure of the described high-pressure homogeneous device of claim 1, it is characterized in that described two guiding gutters extend along a curve respectively, and connect along same tangential direction.
6. according to the Flow guiding structure of the described high-pressure homogeneous device of claim 1, it is characterized in that, described two guiding gutters extend along a curve respectively, and connect along a tangent line direction respectively, this two tangential direction be parallel to each other and standoff distance less than half of each guiding gutter width.
7. according to the Flow guiding structure of the described high-pressure homogeneous device of claim 1, it is characterized in that, the described unit that becomes a mandarin further includes at least one splitter box, is located at described first inner face and has predetermined length, and the one end extends to this two unit that becomes a mandarin and interconnects the place.
8. according to the Flow guiding structure of the described high-pressure homogeneous device of claim 7, it is characterized in that, describedly go out to flow the unit and be communicated with described splitter box with an end that extends to described second inner face.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2005101173456A CN100443152C (en) | 2005-11-02 | 2005-11-02 | High-pressure homogeneous device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2005101173456A CN100443152C (en) | 2005-11-02 | 2005-11-02 | High-pressure homogeneous device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1958139A true CN1958139A (en) | 2007-05-09 |
| CN100443152C CN100443152C (en) | 2008-12-17 |
Family
ID=38070081
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB2005101173456A Active CN100443152C (en) | 2005-11-02 | 2005-11-02 | High-pressure homogeneous device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN100443152C (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104132836B (en) * | 2014-08-08 | 2016-10-26 | 刘宝帅 | Equal pulp grinder and equal sizing process for residue of pesticide detection pretreatment |
| CN109078734A (en) * | 2018-08-07 | 2018-12-25 | 中国农业大学 | Short distance jet stream concurrent crosses the valve that clashes |
| CN110435087A (en) * | 2019-08-09 | 2019-11-12 | 张家港倍恩特磁塑科技有限公司 | Thermosetting property BMC plastic packaging stator plastic packaging mold |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4533254A (en) * | 1981-04-17 | 1985-08-06 | Biotechnology Development Corporation | Apparatus for forming emulsions |
| JP2788010B2 (en) * | 1989-03-31 | 1998-08-20 | ナノマイザー株式会社 | Emulsifier |
| JP3296954B2 (en) * | 1996-01-29 | 2002-07-02 | 株式会社ジーナス | Atomization device and atomization method |
| US5749650A (en) * | 1997-03-13 | 1998-05-12 | Apv Homogenizer Group, A Division Of Apv North America, Inc. | Homogenization valve |
| US5887977A (en) * | 1997-09-30 | 1999-03-30 | Uniflows Co., Ltd. | Stationary in-line mixer |
-
2005
- 2005-11-02 CN CNB2005101173456A patent/CN100443152C/en active Active
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104132836B (en) * | 2014-08-08 | 2016-10-26 | 刘宝帅 | Equal pulp grinder and equal sizing process for residue of pesticide detection pretreatment |
| CN109078734A (en) * | 2018-08-07 | 2018-12-25 | 中国农业大学 | Short distance jet stream concurrent crosses the valve that clashes |
| CN109078734B (en) * | 2018-08-07 | 2020-03-13 | 中国农业大学 | Short-distance jet flow common-point intersection clash valve |
| CN110435087A (en) * | 2019-08-09 | 2019-11-12 | 张家港倍恩特磁塑科技有限公司 | Thermosetting property BMC plastic packaging stator plastic packaging mold |
Also Published As
| Publication number | Publication date |
|---|---|
| CN100443152C (en) | 2008-12-17 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US7878705B2 (en) | Static mixing element and method of mixing a drilling liquid | |
| EP1945337B1 (en) | Eddy chamber | |
| CN1958139A (en) | High-pressure homogeneous device | |
| DE602005005574T2 (en) | Microfluidic chip | |
| EP1549917B1 (en) | Airflow meter with device for the separation of foreign particles | |
| CN1411898A (en) | Pipe fitting with additive material feeding device | |
| EP2924271A1 (en) | Homogenising device for at least two fluid streams, in particular for homogeneous gas-air mixing in a gas engine | |
| CN105944584A (en) | Static mixer for liquid-liquid mixed emulsification and working method thereof | |
| AU687862B2 (en) | System for pumping liquids using a jet pump | |
| EP2161528A3 (en) | Flow guiding element and heat exchanger | |
| EP2739380B1 (en) | Mixing and metering device for mixing and metering chemicals | |
| EP1646847A1 (en) | Device for determining at least one parameter of a medium flowing in a line | |
| CN102917779A (en) | Mixing system comprising an extensional flow mixer | |
| DE102004022271A1 (en) | Device for determining at least one parameter of a medium flowing in a conduit | |
| CN117776392A (en) | Treatment of semi-coke wastewater hybrid multi-stage AO processing system | |
| CN1758003A (en) | A fabric dryer and guiding device and guiding blade | |
| GB2357710A (en) | Mixing oil in a transfer line prior to sampling | |
| EP2321538A1 (en) | Microfluid device | |
| DE102008002363B4 (en) | Fuel cell system and its flow control mechanism | |
| AT521034B1 (en) | Shaping machine with a hydraulic system | |
| DE112011102859T5 (en) | nozzle head | |
| CN104147954B (en) | Blender and mixing arrangement | |
| EP1562001A1 (en) | Venting apparatus | |
| CN101412266A (en) | Adding apparatus and additive chamber for liquid additive | |
| FI111284B (en) | Method and apparatus for introducing a chemical into a liquid stream |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |