CN202762380U - Segmented counter-flow stirrer with fold blades - Google Patents
Segmented counter-flow stirrer with fold blades Download PDFInfo
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- CN202762380U CN202762380U CN 201220367574 CN201220367574U CN202762380U CN 202762380 U CN202762380 U CN 202762380U CN 201220367574 CN201220367574 CN 201220367574 CN 201220367574 U CN201220367574 U CN 201220367574U CN 202762380 U CN202762380 U CN 202762380U
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- oar
- agitator
- segmentation
- adverse current
- hinged joint
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Abstract
The utility model provides a segmented counter-flow stirrer with fold blades. The segmented counter-flow stirrer with fold blades comprises roots, ends, blade connectors and a hub, is of a fold blade structure which is formed according to the special folding process and favorable for allowing fluid to flow through smoothly and reducing loss of a stirring machine, and further is of a special segmented counter-flow structure which is capable of improving stirred fluid to circulate axially in the whole kettle on the condition of low stirring power so as to realize high-efficiency and low-power-consumption mixing effect. The segmented counter-flow stirrer with the fold blades is particularly applicable to liquid/liquid dispersing and heat transfer and solid/liquid suspension of mixing systems of liquids with medium and low viscosity. When applied to the field of mixing of liquid with medium and low viscosity, the segmented counter-flow stirrer with the fold blades can be adaptable to stirring systems for liquid with variable viscosity during process; and further, stable mixing and dispersing effects can be achieved by the stirrers which are in multi-layer combination on the operation condition with change of operating liquid level in the kettle.
Description
Technical field
The utility model relates to a kind of agitating device of low-consumption high-efficiency, in being particularly suitable for, the liquid of the liquid mixed system of low-viscosity/liquid dispersion and heat transfer, solid-liquid suspend.
Background technology
Agitating device is extensive in sector applications such as chemical industry, medicine, usually comes the type of choice for use agitator according to physico-chemical property, stirring purpose and the kettle features of shape etc. of agitated medium, and wherein, the viscosity size of medium is a very important Consideration.
Generally speaking, for the stirring system of middle low-viscosity, the conventional agitator that can Gong select has push type, turbine type, oar formula, anchor formula, frame and screw rod/helical-ribbon type etc.Wherein, propeller agitator can form very strong axial circulation and flow, and the radial flow moment only is suitable for the very low stirring system of viscosity; It is large that anchor formula and gate stirrer stir scope, but the shearing force of slowing down when low is little, and whole still circulation ability is very weak, only is suitable for than the high viscosity system or low glutinous system in take crystallization/conduct heat as purpose; Screw rod/helix(ribbon type) agitator is than the anchor gate stirrer, and partial cut and whole still axial circulation increase, but it is also large to stir power consumption, and the mixing efficiency under middle low viscosity system is not high, generally also only uses under the sticking system of height; Oar formula and turbine agitator have certain axial and Radial Flow, and shear action is stronger, and the axial dispersion effect is also good, can be suitable for middle low viscosity liquid-phase system and solid-liquid suspension system, but power consumption is large, and is less economical.In published patent documentation, also just like hinge paddle type stirrer, be called " a kind of hinge paddle type stirrer " utility model technical scheme such as following No. 201120249964.1 name of the patent No., but still have the large and less economical shortcoming of power consumption.
The utility model content
The purpose of this utility model is to provide a kind of segmentation adverse current hinged joint agitator that can solve conventional agitator deficiency of existence in middle low viscosity stirring system is used.
The technical scheme of taking for achieving the above object is: a kind of segmentation adverse current hinged joint agitator is made of root oar, end oar, blade connection and wheel hub.Root oar and end oar adopt dull and stereotyped, form with specific crooked radian and radius compacting, and blade connection is slotted according to the bending shape of segmentation blade.
As preferred version of the present utility model, the blade of agitator evenly distributes, and quantity is generally 2-4, preferably two.
As preferred version of the present utility model, described segmentation adverse current hinged joint agitator places kettle, and the still of kettle directly is made as DI, the oar of agitator footpath Dj is 40 ~ 98% of still footpath DI, when kettle during with baffle plate, and preferred 40 ~ 60%, when kettle during without baffle plate, preferred 90 ~ 98%; The oar footpath D1 of root oar is 60 ~ 80%, preferred 65 ~ 70% of oar footpath Dj; The length L of end oar is 8 ~ 20%, preferred 12 ~ 15% of oar footpath Dj; The length L of the oar footpath Dj of agitator, the oar footpath D1 of root oar and end oar can be adjusted according to the requirement of stirring operating mode and stirring purpose;
As preferred version of the present utility model, the blade width b1 of the root oar of agitator is 5 ~ 20%, preferred 12% of agitator oar footpath Dj; Root oar radius bend r1 is 10 ~ 20%, preferred 15% of agitator oar footpath Dj; The angle α of root oar placed side and horizontal plane is 30 ~ 60 °, preferred 45 °; Root oar blade width b1, root oar radius bend r1 and root oar angle α can adjust according to the requirement of stirring operating mode and stirring purpose;
As preferred version of the present utility model, the blade width b2 of the end oar of agitator is 3 ~ 15%, preferred 8% of agitator oar footpath Dj; End oar radius bend r2 is 10 ~ 20%, preferred 15% of agitator oar footpath Dj; The angle β of oar placed side, end and horizontal plane is 30 ~ 60 °, preferred 45 °; End oar blade width b2, end oar radius bend r2 and end oar angle β can adjust according to the requirement of stirring operating mode and stirring purpose;
As preferred version of the present utility model, described agitator is generally multi-layer configuration and uses, and is 90 ° between the adjacent layer and staggers.Interlamellar spacing S is 30 ~ 120%, preferred 50 ~ 70% of agitator oar footpath Dj.
The design principle of the segmentation adverse current hinged joint agitator that the utility model provides is that during described agitator rotation, the root oar of blade and end oar advance liquid respectively toward opposite direction, impel liquid to form axial circulation, possess the Field Characteristics of pusher blade.Because blade width is narrower, described agitator is generally multilayer and uses, and stirrer combination is similar to again a discrete ribbon-screw impeller.Therefore, described agitator is suitable for low, middle viscosity liquid system, is particularly suitable for the operation in transition region basin.In the transition region basin, blade nearby has little turbulent area, occasion in multi-layer configuration, the turbulent area of the agitator between adjacent layer can be coupled together, form the axial circulation in the whole still scope, therefore have the mixing efficiency suitable with ribbon-screw impeller, and its power levels number is much smaller than ribbon-screw impeller, therefore the standby efficient mixed effect of described mixing tool; In addition, the blade of described agitator is pressed into arc according to special bending rule, and fluid can further reduce the mechanical loss of described agitator through round and smooth passing through of its when surface.
Another beneficial effect of the segmentation adverse current hinged joint agitator that the utility model provides is, in middle low-viscosity zone, and the stirring system that described agitator can change applicable to the operational process of craft medium viscosity, this is that conventional agitator can not be compared; Secondly, when the operation liquid level in the still changed, the combination of the multi-layer configuration of described agitator also can provide stable mixing and dispersion effect.
Description of drawings
Fig. 1 is front view of the present utility model;
Fig. 2 is the isometric drawing of Fig. 1;
Fig. 3 is that the A of Fig. 1 root oar is to view;
Fig. 4 is the B face view of Fig. 1 end oar;
Fig. 5 is the schematic diagram of multi-layer configuration of the present utility model.
Reference numeral: 1 root oar, 2 blade connections
3 end oars, 4 wheel hubs
The oar footpath of the oar footpath D1 root oar of Dj agitator
The interlamellar spacing of the length S agitator of L end oar
The blade width of the blade width b2 end oar of b1 root oar
The radius bend of the radius bend r2 end oar of r1 root oar
The placed side of α agitator and the angle of horizontal plane
The placed side of β agitator and the angle of horizontal plane.
The specific embodiment
Below in conjunction with accompanying drawing the utility model segmentation adverse current hinged joint agitator is described in further details.
Embodiment 1
Among Fig. 1, segmentation adverse current hinged joint agitator comprises root oar 1, blade connection 2, end oar 3, wheel hub 4.The oar footpath Dj of agitator is 50% of still footpath DI, and the oar footpath D1 of root oar is 67.5% of oar footpath Dj; The length L of end oar is 12% of oar footpath Dj;
Among Fig. 3, the blade width b1 of the root oar of agitator is 12% of agitator oar footpath Dj; Radius bend r1 is 15% of agitator oar footpath Dj; The angle α of placed side and horizontal plane is 45 °;
Among Fig. 4, the blade width b2 of the end oar of agitator is 8% of agitator oar footpath Dj; Radius bend r2 is 15% of agitator oar footpath Dj; The angle β of placed side and horizontal plane is 45 °;
Among Fig. 5, agitator is that three layers of configuration are used, and is 90 ° between the adjacent layer and staggers.Interlamellar spacing S is 60% of agitator oar footpath Dj.
Embodiment 2
Segmentation adverse current hinged joint agitator comprises root oar 1, blade connection 2, end oar 3, wheel hub 4.The oar footpath Dj of agitator is 40% of still footpath DI, and the oar footpath D1 of root oar is 60% of oar footpath Dj; The length L of end oar is 17.5% of oar footpath Dj;
The blade width b1 of the root oar of agitator is 8% of agitator oar footpath Dj; Radius bend r1 is 10% of agitator oar footpath Dj; The angle α of placed side and horizontal plane is 30 °;
The blade width b2 of the end oar of agitator is 5% of agitator oar footpath Dj; Radius bend r2 is 10% of agitator oar footpath Dj; The angle β of placed side and horizontal plane is 30 °;
Agitator is that four layers of configuration are used, and is 90 ° between the adjacent layer and staggers.Interlamellar spacing S is 30% of agitator oar footpath Dj.
Embodiment 3
Segmentation adverse current hinged joint agitator comprises root oar 1, blade connection 2, end oar 3, wheel hub 4.The oar footpath Dj of agitator is 98% of still footpath DI, and the oar footpath D1 of root oar is 80% of oar footpath Dj; The length L of end oar is 8% of oar footpath Dj;
The blade width b1 of the root oar of agitator is 20% of agitator oar footpath Dj; Radius bend r1 is 20% of agitator oar footpath Dj; The angle α of placed side and horizontal plane is 60 °;
The blade width b2 of the end oar of agitator is 12% of agitator oar footpath Dj; Radius bend r2 is 20% of agitator oar footpath Dj; The angle β of placed side and horizontal plane is 60 °;
Agitator is that five layers of configuration are used, and is 90 ° between the adjacent layer and staggers.Interlamellar spacing S is 100% of agitator oar footpath Dj.
Claims (24)
1. segmentation adverse current hinged joint agitator comprises root oar, end oar, blade connection and wheel hub, and described wheel hub is connected with root oar one end, and the described root oar other end is connected with the end oar by described blade connection.
2. segmentation adverse current hinged joint agitator according to claim 1 is characterized in that, the blade of described agitator evenly distributes.
3. described segmentation adverse current hinged joint agitator according to claim 2 is characterised in that, the blade quantity of described agitator one deck or one group is two.
4. segmentation adverse current hinged joint agitator according to claim 1 is characterized in that, the oar footpath Dj of described agitator is 40 ~ 98% of still footpath DI.
5. segmentation adverse current hinged joint agitator according to claim 4 is characterized in that, described segmentation adverse current hinged joint agitator places kettle, and described kettle is provided with baffle plate, and the oar footpath Dj of described agitator is 40 ~ 60% of still footpath DI.
6. segmentation adverse current hinged joint agitator according to claim 4 is characterized in that, described segmentation adverse current hinged joint agitator places kettle, and described kettle is not baffled, and the oar footpath Dj of described agitator is 90 ~ 98% of still footpath DI.
7. segmentation adverse current hinged joint agitator according to claim 1 is characterized in that, the oar footpath D1 of root oar is 60 ~ 80% of oar footpath Dj.
8. segmentation adverse current hinged joint agitator according to claim 7 is characterized in that, the oar footpath D1 of root oar is 65 ~ 70% of oar footpath Dj.
9. segmentation adverse current hinged joint agitator according to claim 1 is characterized in that, the length L of end oar is 8 ~ 20% of oar footpath Dj.
10. segmentation adverse current hinged joint agitator according to claim 9 is characterized in that, the length L of end oar is 12 ~ 15% of oar footpath Dj.
11. segmentation adverse current hinged joint agitator according to claim 1 is characterized in that, the blade width b1 of the root oar of described agitator is 5 ~ 20% of agitator oar footpath Dj.
12. segmentation adverse current hinged joint agitator according to claim 11 is characterized in that, the blade width b1 of the root oar of described agitator is 12% of agitator oar footpath Dj.
13. segmentation adverse current hinged joint agitator according to claim 1 is characterized in that, the blade width b2 of the end oar of described agitator is the 3-15% of agitator oar footpath Dj.
14. segmentation adverse current hinged joint agitator according to claim 13 is characterized in that, the blade width b2 of the end oar of described agitator is 8% of agitator oar footpath Dj.
15. segmentation adverse current hinged joint agitator according to claim 11 is characterized in that, the root oar radius bend r1 of described agitator is 10 ~ 20% of agitator oar footpath Dj.
16. segmentation adverse current hinged joint agitator according to claim 15 is characterized in that, the root oar radius bend r1 of described agitator is 15% of agitator oar footpath Dj.
17. segmentation adverse current hinged joint agitator according to claim 11 is characterized in that the angle α of the placed side of described root oar and horizontal plane is 30 ~ 60 °.
18. segmentation adverse current hinged joint agitator according to claim 17 is characterized in that the angle α of the placed side of described root oar and horizontal plane is 45 °.
19. segmentation adverse current hinged joint agitator according to claim 13 is characterized in that the placed side of described end oar and the angle β of horizontal plane are 30 ~ 60 °.
20. segmentation adverse current hinged joint agitator according to claim 19 is characterized in that the placed side of described end oar and the angle β of horizontal plane are 45 °.
21. the described segmentation adverse current of arbitrary claim hinged joint agitator is characterized in that according to claim 1-20, described agitator is that use is put in multilayer or many assembly, is 90 ° between the adjacent layer and staggers.
22. segmentation adverse current hinged joint agitator according to claim 21 is characterized in that, interlamellar spacing S is 30 ~ 120% of agitator oar footpath Dj.
23. segmentation adverse current hinged joint agitator according to claim 22 is characterized in that, described agitator is three layers or four layers or five layers of configuration use.
24. segmentation adverse current hinged joint agitator according to claim 23 is characterized in that, interlamellar spacing S is 50 ~ 70% of agitator oar footpath Dj.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220367574 CN202762380U (en) | 2012-07-27 | 2012-07-27 | Segmented counter-flow stirrer with fold blades |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220367574 CN202762380U (en) | 2012-07-27 | 2012-07-27 | Segmented counter-flow stirrer with fold blades |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202762380U true CN202762380U (en) | 2013-03-06 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220367574 Expired - Fee Related CN202762380U (en) | 2012-07-27 | 2012-07-27 | Segmented counter-flow stirrer with fold blades |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202762380U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108300649A (en) * | 2018-04-08 | 2018-07-20 | 浙江长城搅拌设备股份有限公司 | Stirring reactor in process of high-density fermentation |
| CN110721607A (en) * | 2019-09-24 | 2020-01-24 | 王绎皓 | Positive and negative thrust paddle |
-
2012
- 2012-07-27 CN CN 201220367574 patent/CN202762380U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108300649A (en) * | 2018-04-08 | 2018-07-20 | 浙江长城搅拌设备股份有限公司 | Stirring reactor in process of high-density fermentation |
| CN110721607A (en) * | 2019-09-24 | 2020-01-24 | 王绎皓 | Positive and negative thrust paddle |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C53 | Correction of patent of invention or patent application | ||
| CB03 | Change of inventor or designer information |
Inventor after: Xiao Honghai Inventor after: Zhang Xiaohuan Inventor after: Zhang Lei Inventor after: Zhan Xiaoqiang Inventor before: Shang Honghai Inventor before: Zhang Xiaohuan Inventor before: Zhang Lei Inventor before: Zhan Xiaoqiang |
|
| COR | Change of bibliographic data |
Free format text: CORRECT: INVENTOR; FROM: SHANG HONGHAI ZHANG XIAOHUAN ZHANG LEI ZHAN XIAOQIANG TO: XIAO HONGHAI ZHANG XIAOHUAN ZHANG LEI ZHAN XIAOQIANG |
|
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20200331 Address after: 200120 third building, 562 Gao Xiang Ring Road, Shanghai, Pudong New Area Patentee after: SHANGHAI MORIMATSU PRESSURE VESSEL Co.,Ltd. Address before: 200137, No. 3270, No. 3166, Laiyang Road, Shanghai, Pudong New Area Patentee before: SHANGHAI MORIMATSU MIXING TECHNOLOGY ENGINEERING EQUIPMENT Co.,Ltd. |
|
| CP03 | Change of name, title or address | ||
| CP03 | Change of name, title or address |
Address after: Workshop 1, building 1, No. 458, Zhongmin Road, Maogang Town, Songjiang District, Shanghai, 201607 Patentee after: Shanghai Senyong Engineering Equipment Co.,Ltd. Address before: Building 3, No. 562, Gaoxiang Ring Road, Pudong New Area, Shanghai, 200120 Patentee before: SHANGHAI MORIMATSU PRESSURE VESSEL Co.,Ltd. |
|
| 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: 20130306 Termination date: 20210727 |