CN2132562Y - Super-fine homogenizer - Google Patents
Super-fine homogenizer Download PDFInfo
- Publication number
- CN2132562Y CN2132562Y CN 92218302 CN92218302U CN2132562Y CN 2132562 Y CN2132562 Y CN 2132562Y CN 92218302 CN92218302 CN 92218302 CN 92218302 U CN92218302 U CN 92218302U CN 2132562 Y CN2132562 Y CN 2132562Y
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- CN
- China
- Prior art keywords
- stop valve
- homogenizer
- high pressure
- fine
- threeway
- 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.)
- Expired - Fee Related
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- 239000000463 material Substances 0.000 claims abstract description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 7
- 239000011230 binding agent Substances 0.000 claims description 3
- 230000008676 import Effects 0.000 claims description 3
- 238000007599 discharging Methods 0.000 claims description 2
- 239000000203 mixture Substances 0.000 abstract description 8
- 229910052500 inorganic mineral Inorganic materials 0.000 abstract description 6
- 239000007788 liquid Substances 0.000 abstract description 6
- 239000011707 mineral Substances 0.000 abstract description 6
- 230000008901 benefit Effects 0.000 abstract description 2
- 238000000265 homogenisation Methods 0.000 abstract description 2
- 229910052755 nonmetal Inorganic materials 0.000 abstract 2
- 230000000903 blocking effect Effects 0.000 abstract 1
- 230000007547 defect Effects 0.000 abstract 1
- 238000010008 shearing Methods 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- PNEYBMLMFCGWSK-UHFFFAOYSA-N Alumina Chemical compound [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 3
- 239000013078 crystal Substances 0.000 description 3
- 238000010298 pulverizing process Methods 0.000 description 3
- 239000005995 Aluminium silicate Substances 0.000 description 2
- 229910021536 Zeolite Inorganic materials 0.000 description 2
- MCMNRKCIXSYSNV-UHFFFAOYSA-N Zirconium dioxide Chemical compound O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 description 2
- 235000012211 aluminium silicate Nutrition 0.000 description 2
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 229910052900 illite Inorganic materials 0.000 description 2
- NLYAJNPCOHFWQQ-UHFFFAOYSA-N kaolin Chemical compound O.O.O=[Al]O[Si](=O)O[Si](=O)O[Al]=O NLYAJNPCOHFWQQ-UHFFFAOYSA-N 0.000 description 2
- 239000010410 layer Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000010445 mica Substances 0.000 description 2
- 229910052618 mica group Inorganic materials 0.000 description 2
- VGIBGUSAECPPNB-UHFFFAOYSA-L nonaaluminum;magnesium;tripotassium;1,3-dioxido-2,4,5-trioxa-1,3-disilabicyclo[1.1.1]pentane;iron(2+);oxygen(2-);fluoride;hydroxide Chemical compound [OH-].[O-2].[O-2].[O-2].[O-2].[O-2].[F-].[Mg+2].[Al+3].[Al+3].[Al+3].[Al+3].[Al+3].[Al+3].[Al+3].[Al+3].[Al+3].[K+].[K+].[K+].[Fe+2].O1[Si]2([O-])O[Si]1([O-])O2.O1[Si]2([O-])O[Si]1([O-])O2.O1[Si]2([O-])O[Si]1([O-])O2.O1[Si]2([O-])O[Si]1([O-])O2.O1[Si]2([O-])O[Si]1([O-])O2.O1[Si]2([O-])O[Si]1([O-])O2.O1[Si]2([O-])O[Si]1([O-])O2 VGIBGUSAECPPNB-UHFFFAOYSA-L 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000010457 zeolite Substances 0.000 description 2
- 101100532451 Rattus norvegicus Slc22a17 gene Proteins 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 239000011195 cermet Substances 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 239000002537 cosmetic Substances 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 235000013365 dairy product Nutrition 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- -1 hard Raolinite Chemical compound 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 239000011229 interlayer Substances 0.000 description 1
- 238000009527 percussion Methods 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 239000011800 void material Substances 0.000 description 1
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- Disintegrating Or Milling (AREA)
Abstract
The utility model discloses a non-metal mineral super-fine homogenizer, and the existing high pressure homogenizer has the defects of complicated structure, small handling quantity, low efficiency, etc. The device provided by the utility model mainly comprises a high-pressure water inlet pipe 3, high-pressure material tanks 22 and 23, helix nozzles 9 and 18 and blocking harrows 10 and 19. The non-metal mineral super-fine homogenizer can effectively proceed the super-fine comminution and homogenization of the solid-liquid and liquid-liquid mixture. The utility model has the advantages of simple structure, low cost, continuous work and large processing quantity.
Description
The utility model relates to a kind of ultra-fine homogenizer, and it is mainly used in the field such as ultra-fine, pulverizing, homogenize of nonmetallic mineral, medicine, chemical industry, cosmetics and dairy products food processing.
At present, homogenizer is the dispersion that is used for solid-liquid or liquid-liquid two-phase mixture, the work that the homogenize process is mainly used to replace ball mill.
At present, the delaminating of nonmetallic mineral, ultra-fine production efficiency of equipment, ultra-fine disposal ability are poor, and the high pressure homogenizer that German AKW company produces mainly is to adopt reciprocating piston and spring shaft that pressure is provided, thereby ore pulp is among the high pressure.The high pressure ore pulp is extruded and is injected on the normal pressure impeller with very high speed by a tiny linear nozzle, by means of phase mutual friction, the shear action of extruding ore pulp when spraying, and ore pulp is injected in the powerful impulsive force that is produced on the normal pressure impeller, make the hydrogen bond rupture between processed nonmetallic mineral crystal layer, thereby reach the purpose of delaminating with ultra-fine processing.But this equipment only can be used for the kaolinic processing of delaminating, and the reciprocating piston and the required material quality of spring shaft of pressure is provided, and withstand voltage properties requires very high, and treating capacity is little simultaneously, involves great expense.The high pressure homogenizer that Denmark APVRASNNIEA/S enterprise produces mainly is made up of " high-pressure piston pump, homogenize valve, valve body " several parts, material to be processed is forced into 100-1000bar by high-pressure piston pump, reduce pressure by the homogenize valve then and produce very high shearing force suddenly, thereby reach broken solid granule, make the homogenize of solid-liquid two-phase become steady suspension.Because operating pressure height, and the variation of boosting and reducing pressure arranged, so require the ability of high pressure resistant and withstand voltage change of its each component devices higher, be mostly to utilize the zirconia cermet after the fine finishining to make the homogenize valve, make the piston boit of high-pressure piston pump with aluminium oxide ceramics.This makes very difficulty of equipment processing, and cost is higher.And for preventing vibration under the high pressure, noise and valve body cracking phenomena, optional equipment and structure are more, thereby increased the complexity of whole system.
The purpose of this utility model requires defectives such as height, treating capacity is little, efficient is low to propose for complex structure, cost height, the equipment material that solves existing high pressure homogenizer existence just.
Technical solution of the present utility model is to utilize water under high pressure as power, processed nonmetallic mineral or other solid, liquid substance are mixed in a high-pressure-resistant vessel with water under high pressure be co-located in high pressure conditions, make mixture enter a spiral line type nozzle then, mixture under high pressure moves in the helix runner of nozzle fast, thereby produces powerful shearing force and frictional force.These power make very rapidly destroyed its crystal layer structure of substance to be processed, thereby reach the purpose of ultra-fine, pulverizing, homogenize, for further improving ultra-fine, homogenize efficient, in the utility model solution, also be provided with the shelves rake at nozzle exit, so that the jet of high speed extrusion nozzle outlet is reduced suddenly by pressure and collide the shelves rake and the void effect and the powerful impulsive force that produce, further pulverize, the homogenize substance to be processed.
Embodiment is elaborated below in conjunction with the utility model:
Fig. 1 is the structural representation of the utility model embodiment one.
Fig. 2 is the structural representation of the utility model embodiment two.
Fig. 3 is a nozzle arrangements schematic diagram in the utility model.
As shown in Figure 1, water under high pressure after boosted passes stop valve 2,12 and 4,13 successively by water inlet pipe 3 and enters in the upper and lower two- supremes binder jar 22,23 and mix with added pending material after threeway 1 shunting, after high-pressure mixture is by the stop valve 8,17 that links with upper and lower high pressure batch can 22,23 and nozzle 9,18 respectively, store in and under high pressure enter respectively in the spiral line type nozzle 9,18, and along the 36 high speed sinuous movements of spiral line type conduit.At a high speed, high pressure brings very big shearing force and frictional force for mixture in nozzle 9,18.The jet that is penetrated by 9,18 outlets of spiral line type nozzle passes plate washer 11,20 percussions on shelves rake 10,19, by the mixture impulsive force that the shearing force, frictional force and the impact shelves rake that produce produce of in nozzle, moving, can destroy the crystal interlayer structure of material very effectively, thus reach delaminate, ultra-fine, homogenization.The pipeline that Fig. 1 mesohigh batch can 22,23 tops are controlled by stop valve 5,14 respectively is as the usefulness of opening high pressure batch can front exhaust; The pipeline that links to each other with stop valve 7,16 that is positioned at high pressure batch can 22,23 bottoms is mainly used in discharging; The pipeline of stop valve 6,15 controls is reinforced usefulness, and series connection is used in the time of can also being used for connecting a plurality of batch can with the pipeline of stop valve 8,17 controls simultaneously.
In Fig. 1, connect upper and lower two groups of parallel equipment by threeway 1, its objective is that when a high pressure batch can job, another is used for charging, waits to boost, otherwise also identical for entire work process can be carried out continuously.
As shown in Figure 2, the utility model embodiment two and embodiment one difference are: increase by a threeway 21,24 respectively on the pipeline of 2,12 and 4,13 of stop valves, an end of threeway 21,24 is coupled to upper and lower high pressure batch can 22,23 side-lowers respectively with stop valve 25,26 by the road.Set up this pipeline and be to solving when 22,23 work of high pressure batch can, can press knot because of deadweight, bonding at the big or dispersed relatively poor medium of some proportions of jar inner bottom part and locate exporting the aperture, cause and harden and stop up batch can bottom outlet mouth, and influence operate as normal.
By accompanying drawing 3 as can be known, the screw type nozzle 9,18 that the utility model adopts mainly is made up of conical plug 34 and the taper sheath 35 that matches with it, and the length of conical plug 34 is generally 10-1000mm; Be processed with the spiral channel 36 of different cross section profile of tooth on conical plug 34, its pitch is 5-600mm, and the import sectional area A of nozzle 9,18 is 2-15 with the ratio of discharge area B.
The utility model is under the 100-1000bar in operating pressure, adopts the different cross section shape, and pitch and conical plug length are successively carried out ultra-fine grinding to soft kaolin, hard Raolinite, zeolite, illite, mica etc., and its result is:
1. soft kaolin: when feeding granularity is 100 orders, under 300bar pressure, delaminate, after the ultra-fine processing, in the product through disposable.-2 microns content are more than the 85-95%, and-10 microns content reach 100%.Can improve product-2 micron content is more than 80%.
2. coal hard Gao Yanling: when feeding granularity is 200 orders, under 500bar pressure, through disposable delaminate ultra-fine after ,-2 microns content are more than the 67-85% in the product ,-10 microns content reach 100%, can improve product-2 micron content more than 65%.
3. zeolite: when feeding granularity is 100 orders, under 400bar pressure, it is carried out-2 microns content are more than the 75-80% in the disposable ultra-fine treatment product ,-10 microns content reaches 100%, and can to improve product-2 micron content be more than 70%.
4. illite: when feeding granularity is 100 orders, under 650bar pressure, it is carried out the disposable ultra-fine processing of delaminating ,-2 microns content are more than the 80-85% in the product, and-10 microns content reach 100%, and can improve product-2 micron content is more than 75%.
5. mica: when feeding granularity is 80 orders, under 800bar pressure, it is carried out the disposable ultra-fine processing of delaminating ,-2 microns content are more than the 35-65% in the product, and-2 microns content reach 100%, and can improve product-2 micron content is more than 50%.
This shows that the utility model is ultra-fine, pulverizing, homogenize effect are remarkable, and have simple in structure, production cost is low, easy operating, the advantage such as can work long hours continuously is a kind of more satisfactory, is easy to the ultra-fine homogenize equipment of popularizing and promoting.
Claims (3)
1, a kind of superfine homogenizer, it is characterized in that: it is mainly by water inlet pipe 3, upper and lower two-supremes binder jar 22,23, spiral line type nozzle 9,18 and shelves rake 10,19 are formed, water inlet pipe 3 links with threeway 1, connecting line is in upper and lower two-supremes binder jar 22,23 upper ends respectively through stop valve 2,12 and 4,13 at the other two ends of threeway 1, and high pressure batch can 22,23 low apertures link through stop valve 8,17 and 9,18 imports of spiral line type nozzle; 9,18 outlets of screw type nozzle are coupled to plate washer 11,20 and relative with shelves rake 10,19, in addition, are respectively equipped with the gas exhaust piping of being controlled by stop valve 5,14 in pressure pan 22,23 upper ends; The lower end is respectively equipped with by the discharging pipeline of stop valve 7,16 controls and the intake line for the treatment of ultra-fine homogenize material by stop valve 6,15 controls that links to each other with high pressure batch can 22,23 upper side;
2, the described superfine homogenizer of claim 1 is characterized in that: on 2,12 and 4,13 pipelines of stop valve a threeway 21,24 is set respectively.Threeway 21,24 1 brings out mouthful with one and is linked by stop valve 25,26 controls and the pipeline that links to each other with high pressure batch can 22,23 side lower ends.
3, the described superfine homogenizer of claim 1 is characterized in that: spiral line type nozzle the 9, the 18th, form by conical plug 34 and the taper sheath 35 that matches with it, and be processed with the spiral channel 36 of different cross section profile of tooth on the conical plug 34.Wherein conical plug is about and is that 10-1000mm, the pitch of spiral channel 36 are 5-600mm; The import sectional area A of spiral yarn shaped nozzle 9,18 is 2-15 with the ratio of discharge area B.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 92218302 CN2132562Y (en) | 1992-07-08 | 1992-07-08 | Super-fine homogenizer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 92218302 CN2132562Y (en) | 1992-07-08 | 1992-07-08 | Super-fine homogenizer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2132562Y true CN2132562Y (en) | 1993-05-12 |
Family
ID=33765853
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 92218302 Expired - Fee Related CN2132562Y (en) | 1992-07-08 | 1992-07-08 | Super-fine homogenizer |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2132562Y (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100406127C (en) * | 2006-08-30 | 2008-07-30 | 西安理工大学 | Combined hydraulic ultrafine powder grinding device |
| CN101961616A (en) * | 2010-10-20 | 2011-02-02 | 合肥开尔纳米能源科技股份有限公司 | Liquid phase dispersion device of nano-powder material |
| CN103331199A (en) * | 2013-07-15 | 2013-10-02 | 南京奥利佳水刀制造有限公司 | Extra high pressure homogenizer |
| CN112125314A (en) * | 2020-09-21 | 2020-12-25 | 湖南御家化妆品制造有限公司 | Illite and preparation method and application thereof |
-
1992
- 1992-07-08 CN CN 92218302 patent/CN2132562Y/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100406127C (en) * | 2006-08-30 | 2008-07-30 | 西安理工大学 | Combined hydraulic ultrafine powder grinding device |
| CN101961616A (en) * | 2010-10-20 | 2011-02-02 | 合肥开尔纳米能源科技股份有限公司 | Liquid phase dispersion device of nano-powder material |
| CN101961616B (en) * | 2010-10-20 | 2013-09-18 | 合肥开尔纳米能源科技股份有限公司 | Liquid phase dispersion device of nano-powder material |
| CN103331199A (en) * | 2013-07-15 | 2013-10-02 | 南京奥利佳水刀制造有限公司 | Extra high pressure homogenizer |
| CN112125314A (en) * | 2020-09-21 | 2020-12-25 | 湖南御家化妆品制造有限公司 | Illite and preparation method and application thereof |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C15 | Extension of patent right duration from 15 to 20 years for appl. with date before 31.12.1992 and still valid on 11.12.2001 (patent law change 1993) | ||
| RN01 | Renewal of patent term | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 1993.05.12 |