CN201815309U - Gate type agitator with lower large blade and openings for reaction kettle - Google Patents
Gate type agitator with lower large blade and openings for reaction kettle Download PDFInfo
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- CN201815309U CN201815309U CN2010205569514U CN201020556951U CN201815309U CN 201815309 U CN201815309 U CN 201815309U CN 2010205569514 U CN2010205569514 U CN 2010205569514U CN 201020556951 U CN201020556951 U CN 201020556951U CN 201815309 U CN201815309 U CN 201815309U
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Abstract
The utility model provides a gate type agitator with a lower large blade and openings for a reaction kettle, which is used in chemical engineering equipment and particularly suitable for reaction kettles for high-viscosity material reaction in chemical engineering equipment. The gate type agitator adopts the technical scheme that a stir frame is arranged on the stirring shaft of a reaction kettle; the stir frame comprises transverse and vertical spokes which are mounted on and surround the stirring shaft; a stir large blade is arranged at the lower end of the stir frame and at the bottom of the reaction kettle; and openings in a porosity diameter lager than 5mm are formed on the transverse and vertical spokes of the stir frame and the lower large blade; and the opening area on the lower large blade is lager than 25%.
Description
Technical field:
A kind of reactor is used for chemical equipment with underlying Da Ye perforate gate stirrer, is particularly useful for the reactor of reaction treatment high-viscosity material in the chemical equipment.
Background technology:
At present, various reactors adopt frame with agitator more, the oar formula, forms such as anchor formula, stirring reaction for some high-viscosity materials, as polyacrylate polymerisation etc., it is very strict that it stirs requirement, require to stir very even, because the polyacrylate polymerisation often adopts mass polymerization or solution polymerization process, its course of reaction medium viscosity changes greatly, count to very high centipoise number from initial very low centipoise, so traditional alr mode often causes stirring inhomogeneous, insufficient, even because the too high high-viscosity material " poly-group " that causes of material viscosity, traditional alr mode can not make it fully to mix with material on every side, various additives thereby do not enter reaction zone fully.
Summary of the invention:
Providing of the purpose of this utility model a kind ofly can promote that course of reaction is complete, the reactor stirring system that adapts to various viscosity, its main implementation technique scheme is such: the stirring frame is set on the reactor shaft, described stirring frame is axis of rotation with the shaft, its plane should be straight in shaft, its surfaces of revolution should be consistent with reactor round inwall, and described stirring frame is made up of banner bar and vertical scroll of painting or calligraphy bar, around being installed on the shaft.
The place sets to put and stirs Da Ye bottom the close reactor in stirring frame lower end, and described underlying stirring Da Ye is axis of rotation with the shaft, and its plane is answered straight in shaft, and its surfaces of revolution should match with circular still Bottom Shape.
On described stirring frame banner bar, tight width of cloth bar and underlying stirring Da Ye, establish perforate, described perforate cell size diameter should be greater than 5mm, the perforated area zone should be greater than 25% on above-mentioned underlying stirring Da Ye, like this, during device busy described in the utility model because the perforate on frame and the Da Ye, in stirring, can in time break " the poly-group " of high-viscosity material, significantly reduce the load moment when stirring simultaneously.
The novel advantage of this reality is to have guaranteed some polymerisation in bulks with a kind of simple structure, polymerisation in solution such as polypropylene synthetic reaction etc., and material viscosity changes greatly, and material viscosity uneven easily " poly-group " makes to react completely and effectively evenly.
Description of drawings:
Accompanying drawing 1 is the utility model structural representation;
Wherein: (1) reactor, (2) shaft, (3) stir frame, (4) banner bar, (5) vertical scroll of painting or calligraphy bar, (6) perforate, Da Ye is stirred in (7) underlying.
The specific embodiment:
As shown in Figure 1, on the shaft (2) of reactor (1), be provided with and stir frame (3), described stirring frame (3) is an axis of rotation with shaft (2), its plane should be straight in shaft (2), its surfaces of revolution should be consistent with reactor (1) drum shape inwall, described stirring frame (3) is made up of banner bar (4) and vertical scroll of painting or calligraphy bar (5), around being installed on the shaft (2).
The place sets to put and stirs Da Ye (7) bottom the close reactor in stirring frame (3) lower end, it is axis of rotation with shaft (2) that Da Ye (7) is stirred in described underlying, its plane should be straight in shaft (2), and its surfaces of revolution should match with the circular still Bottom Shape of reactor (1).
Establish perforate (6) on described stirring frame (3) banner bar (4), vertical scroll of painting or calligraphy bar (5) and underlying stirring Da Ye (7), described perforate (6) cell size diameter should be greater than 5mm, and upward perforate (6) surface area should be greater than 25% to stir Da Ye (7) in above-mentioned underlying.
Claims (3)
1. a reactor is with underlying Da Ye perforate gate stirrer, comprise: Da Ye is stirred in reactor, shaft, stirring frame, banner bar, vertical scroll of painting or calligraphy bar, perforate, underlying, it is characterized in that: the stirring frame is set on the reactor shaft, the place sets to put and stirs Da Ye bottom the close reactor in stirring frame lower end, it is axis of rotation with the shaft that Da Ye is stirred in described underlying, its plane should be straight in shaft, and its surfaces of revolution should match with circular still Bottom Shape.
2. according to the described a kind of reactor of claim 1 underlying Da Ye perforate gate stirrer, it is characterized in that: stir on the Da Ye in banner bar, vertical scroll of painting or calligraphy bar and the underlying of described stirring frame and establish perforate, described perforate cell size diameter should be greater than 5mm, and the perforated area zone should be greater than 25% on above-mentioned underlying stirring Da Ye.
3. according to the described a kind of reactor of claim 1 underlying Da Ye perforate gate stirrer, it is characterized in that: described stirring frame is made up of banner bar and vertical scroll of painting or calligraphy bar, around being installed on the shaft.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010205569514U CN201815309U (en) | 2010-10-12 | 2010-10-12 | Gate type agitator with lower large blade and openings for reaction kettle |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010205569514U CN201815309U (en) | 2010-10-12 | 2010-10-12 | Gate type agitator with lower large blade and openings for reaction kettle |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201815309U true CN201815309U (en) | 2011-05-04 |
Family
ID=43913281
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010205569514U Expired - Fee Related CN201815309U (en) | 2010-10-12 | 2010-10-12 | Gate type agitator with lower large blade and openings for reaction kettle |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201815309U (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102229885A (en) * | 2011-06-17 | 2011-11-02 | 吉武科 | Stirrer for fermentation of high-viscosity materials |
| CN102343230A (en) * | 2011-08-08 | 2012-02-08 | 能一郎科技股份有限公司 | Mixer for preparing lithium-ion battery electrolyte |
| CN102688623A (en) * | 2012-06-14 | 2012-09-26 | 长沙中联重科环卫机械有限公司 | Material heating device |
| CN109070023A (en) * | 2017-01-03 | 2018-12-21 | 株式会社Lg化学 | Dissolve mixer |
| CN115320903A (en) * | 2022-10-14 | 2022-11-11 | 溧阳市宇峰新材料有限公司 | Filling equipment for sealant and using method thereof |
-
2010
- 2010-10-12 CN CN2010205569514U patent/CN201815309U/en not_active Expired - Fee Related
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102229885A (en) * | 2011-06-17 | 2011-11-02 | 吉武科 | Stirrer for fermentation of high-viscosity materials |
| CN102343230A (en) * | 2011-08-08 | 2012-02-08 | 能一郎科技股份有限公司 | Mixer for preparing lithium-ion battery electrolyte |
| CN102688623A (en) * | 2012-06-14 | 2012-09-26 | 长沙中联重科环卫机械有限公司 | Material heating device |
| CN109070023A (en) * | 2017-01-03 | 2018-12-21 | 株式会社Lg化学 | Dissolve mixer |
| US11033865B2 (en) | 2017-01-03 | 2021-06-15 | Lg Chem, Ltd. | Dissolution mixer |
| CN115320903A (en) * | 2022-10-14 | 2022-11-11 | 溧阳市宇峰新材料有限公司 | Filling equipment for sealant and using method thereof |
| CN115320903B (en) * | 2022-10-14 | 2023-02-03 | 溧阳市宇峰新材料有限公司 | Filling equipment for sealant and using method thereof |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20110504 Termination date: 20121012 |