CN102085460A - Disperse emulsifying machine - Google Patents
Disperse emulsifying machine Download PDFInfo
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- CN102085460A CN102085460A CN2009102538821A CN200910253882A CN102085460A CN 102085460 A CN102085460 A CN 102085460A CN 2009102538821 A CN2009102538821 A CN 2009102538821A CN 200910253882 A CN200910253882 A CN 200910253882A CN 102085460 A CN102085460 A CN 102085460A
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- flow path
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Abstract
The invention discloses a disperse emulsifying technology, wherein the pressure in a device can be adjusted and controlled; and a treated object can be subjected to stirring and disperse processing for any times repeatedly in the device so as to improve the uniformity of the particles.
Description
Affiliated technical field
The present invention relates to rotary impact type dispersion and emulsion technology.
Background technology
Rotary dispersion and emulsion device is being widely used in industrial circle.Device in the past generally all is to resemble suction inlet to be arranged the centrifugal water pump, the rotor that has vanelets the impeller that resembles centrifugal pump is arranged in the casing, rotor turns round then, and material just is inhaled in the casing, and obtain centrifugal force there from epitrochanterian vanelets, material flies away from rotor and bumps against with the stator that is arranged on the rotor outer ring and be broken, disperse, stir under centrifugal action, subsequently, material is discharged from outlet under the effect of the pressure that centrifugal force transforms.
In order to obtain the dispersive property of particle size homogeneous, rotor and stator often resemble makes multistage form the multistage pump, also often employing will be from entering the material of recycling can after dispersal device is handled, and the method that the suction inlet by recycling can and dispersal device joins imports dispersal device again and carries out repeatedly the homogeneity that dispersion treatment improves particle size.But after the employing multi-stage rotor form, device can produce high pressure just as multistage pump, and the needed cooling water of the mechanical seal of device also must improve hydraulic pressure, and the supply-water pump that is used for supercharging will become necessary auxiliary device.In addition, import the method that dispersal device carries out repeatedly dispersion treatment again by recycling can, system becomes open, and it is difficult that the continuous production of closed conduct will become.
It is controlled to the invention provides a kind of interior pressure of device that makes, save the dispersion processing method of mechanical seal supply-water pump with reducing the pressure in the device, also provide a kind of when being used for closed conduit and producing simultaneously, material by recycling can in the inner repeatedly dispersion processing method of cyclic process of not carrying out arbitrarily of device.
Have the such function of water pump so rotary dispersion and emulsion device produces centrifugal force when turning round owing to rotor, the principle of dispersal device in the past can be showed as shown in Figure 3, and principle of the present invention can be showed as shown in Figure 1.Promptly, as construct shown in Figure 4, a circulation flow path of going back that connects the stator inside and outside circle is set in the front of the chopped-off head stator 2-2 that has dispersal device now, go back the suction inlet that circulation flow path also flows into chopped-off head rotor 1-2 from the object being treated that final stage rotor 1-1 comes out by this, thereby make pressure obtain at the suction inlet place discharging.
The invention has the beneficial effects as follows, since be provided with in the front of chopped-off head stator 2-2 connect the stator inside and outside circle go back circulation flow path 6, can go back the suction inlet release pressure of circulation flow path by this from the object being treated that final stage rotor 1-1 comes out, so the pressure in the casing just can be controlled in the gap of going back circulation flow path by adjusting at the chopped-off head rotor.In addition, the material of being gone back stream sucks by dispersed with stirring once more from the suction inlet of chopped-off head rotor 1-2, can improve the homogeneous performance of particle.
Description of drawings
The present invention is further described below in conjunction with drawings and Examples
Fig. 1 is a schematic diagram of the present invention
Fig. 2 is the schematic diagram that the present invention is provided with non-return valve
Fig. 3 is the schematic diagram of dispersion and emulsion in the past
Fig. 4 is the sectional structure chart of first embodiment of the invention
Fig. 5 is the sectional structure chart that the present invention is provided with barrier plate
Fig. 6 is the structure chart that the present invention is provided with non-return valve
Fig. 7 is the structure chart that the present invention adopts piston to regulate to go back the circulation flow path gap
1-1. final stage rotor among the figure, 1-2. chopped-off head rotor, 2-1. final stage stator, 2-2. chopped-off head stator, 3. outlet, 4. spool, 5. casing is 6. gone back circulation flow path, 7. barrier plate, 8. classification hole, 9. non-return valve, 10. screw thread, 11. suction lines, 12. pistons.
The specific embodiment
In Fig. 4, apparatus of the present invention are fixed with casing 5 on support, fixing stator 2 is arranged in the casing, casing 5 li in addition can be free rotating 4, is equipped with the rotating rotor 1 of axle, in addition on the axle, the front of chopped-off head stator 2-2, be provided with connect circle and cylindrical in the stator go back circulation flow path 6, can go back the suction inlet that circulation flow path 6 enters chopped-off head rotor 1-2 by this from the object being treated that final stage rotor 1-1 comes out, regulate this gap of going back circulation flow path and just can control the interior pressure of casing.
Shown in Figure 6 is that apparatus of the present invention are controlled the embodiment of casing internal pressure by non-return valve is set.The intensity that changes the spring of non-return valve 10 among the figure just can the interior pressure of control device.
Shown in Figure 5 is the embodiment that is provided with barrier plate 7 and classification hole 8.Never grade material that the dispersed with stirring that rotor 1-1 comes out is crossed flows while turning round to outlet in casing, the distribution of material will decide according to the weight of particle on its turning circle, the particle centrifugal force senior general that weight is big is distributed in the outside of turning circle, the material that the distributed granule size is different on the therefore different tactical diameters.As shown in Figure 5, the right side of outlet 3 contact circulation flow paths is moved, between going back circulation flow path 6 and exporting 3, barrier plate 7 is set, offer classification hole 8 on the barrier plate 7, radial position according to classification hole 8 can only allow the material that is distributed on this tactical diameter pass through, and that is to say the material that can obtain our needed grain size by the position of setting classification hole 8.
Also the gap adjustment of circulation flow path 6 is to adopt helicitic texture to realize in Fig. 5 embodiment, and Fig. 7 demonstration is to adopt piston push-and-pull suction line to realize the embodiment that regulates.The circulation flow path gap of going back that is conditioned can be as shown in Figure 5 a conical surface shape, also can be flat shape as shown in Figure 7.
Claims (4)
1. rotary-type dispersion and emulsion technology.On support, be fixed with casing 5, casing has fixing stator 2 for 5 li, casing 5 li in addition can be free rotating 4, be equipped with the rotating rotor 1 of axle on the axle, it is characterized in that: the front of chopped-off head stator 2-2, be provided with connect circle and cylindrical in the stator go back circulation flow path 6, can go back the suction inlet that circulation flow path 6 enters chopped-off head rotor 1-2 by this from the object being treated that final stage rotor 1-1 comes out, regulate this gap of going back circulation flow path and just can control the interior pressure of casing.
2. rotary dispersion and emulsion technology according to claim 1 is gone back circulation flow path at it and non-return valve 9 can be set be controlled pressure in the casing one of for its feature.
3. according to claim 1 and 2 described rotary dispersion and emulsion technology, its outlet 3 is arranged on the front of going back circulation flow path, between going back circulation flow path 6 and exporting 3, barrier plate 7 is set, offer classification hole 8 on the barrier plate 7, can allow only according to the position in classification hole 8 rotating material is passed through on the radial location in this hole, thus reach grading effect be configured to one of its feature.
4. according to claim 1 and 3 described rotary dispersion and emulsion technology, its shape of going back the circulation flow path gap can also can be the plane for the conical surface, and the adjusting in its gap can adopt helicitic texture also can adopt cylinder or oil cylinder push-and-pull suction line to be embodied as one of its feature.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009102538821A CN102085460A (en) | 2009-12-02 | 2009-12-02 | Disperse emulsifying machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009102538821A CN102085460A (en) | 2009-12-02 | 2009-12-02 | Disperse emulsifying machine |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN102085460A true CN102085460A (en) | 2011-06-08 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2009102538821A Pending CN102085460A (en) | 2009-12-02 | 2009-12-02 | Disperse emulsifying machine |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN102085460A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103506028A (en) * | 2012-06-28 | 2014-01-15 | 上海顺跃精密机械有限公司 | Rotary disperser |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0673677A1 (en) * | 1992-11-02 | 1995-09-27 | KLADOV, Anatoly Fedorovich | Ultrasonic activator |
| CN2565532Y (en) * | 2002-07-19 | 2003-08-13 | 金学刚 | Multi-material mixed emulsion machine |
| CN2714140Y (en) * | 2004-08-09 | 2005-08-03 | 太仓液压元件有限公司 | Pipe line type high-shearing emulsifier |
| US7293909B2 (en) * | 2002-09-25 | 2007-11-13 | Reika Kogyo Kabushiki Kaisha | Apparatus and method for mixing by agitation in a multichambered mixing apparatus including a pre-agitation mixing chamber |
-
2009
- 2009-12-02 CN CN2009102538821A patent/CN102085460A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0673677A1 (en) * | 1992-11-02 | 1995-09-27 | KLADOV, Anatoly Fedorovich | Ultrasonic activator |
| CN2565532Y (en) * | 2002-07-19 | 2003-08-13 | 金学刚 | Multi-material mixed emulsion machine |
| US7293909B2 (en) * | 2002-09-25 | 2007-11-13 | Reika Kogyo Kabushiki Kaisha | Apparatus and method for mixing by agitation in a multichambered mixing apparatus including a pre-agitation mixing chamber |
| CN2714140Y (en) * | 2004-08-09 | 2005-08-03 | 太仓液压元件有限公司 | Pipe line type high-shearing emulsifier |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103506028A (en) * | 2012-06-28 | 2014-01-15 | 上海顺跃精密机械有限公司 | Rotary disperser |
| CN103506028B (en) * | 2012-06-28 | 2015-11-25 | 南通中元实业有限公司 | Rotary disperser |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| ASS | Succession or assignment of patent right |
Owner name: SHANGHAI SHUNYUE PRECISION MACHINERY CO., LTD. Free format text: FORMER OWNER: NANTONG ZHONGYUAN INDUSTRY CO., LTD. Effective date: 20120718 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| COR | Change of bibliographic data |
Free format text: CORRECT: ADDRESS; FROM: 226006 NANTONG, JIANGSU PROVINCE TO: 200233 MINHANG, SHANGHAI |
|
| TA01 | Transfer of patent application right |
Effective date of registration: 20120718 Address after: 200233 room 26, building 1618, No. 518, Minhang District, Shanghai, Yishan Road Applicant after: Shanghai Shunyue Precision Machinery Co., Ltd. Address before: 226006 No. 44, Hong Kong Road, Nantong, Jiangsu Applicant before: Nantong Zhongyuan Industrial Co., Ltd. |
|
| DD01 | Delivery of document by public notice |
Addressee: Cheng Zhongyuan Document name: Notification of Passing Examination on Formalities |
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| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| DD01 | Delivery of document by public notice |
Addressee: Shanghai Shunyue Precision Machinery Co., Ltd. Document name: the First Notification of an Office Action |
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| C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20110608 |