CN200939378Y - High speed reactor - Google Patents
High speed reactor Download PDFInfo
- Publication number
- CN200939378Y CN200939378Y CN 200620063107 CN200620063107U CN200939378Y CN 200939378 Y CN200939378 Y CN 200939378Y CN 200620063107 CN200620063107 CN 200620063107 CN 200620063107 U CN200620063107 U CN 200620063107U CN 200939378 Y CN200939378 Y CN 200939378Y
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- CN
- China
- Prior art keywords
- kettle
- axle
- stirring
- shaft
- high speed
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- 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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- Mixers Of The Rotary Stirring Type (AREA)
Abstract
The utility model relates to a chemical production equipment, in particular to a high speed reactor used for dehydrating and mixing the acidic base material during producing the glass cement. The high speed reactor is composed of a kettle, a mixer shaft, and an agitating vane which is arranged on the mixer shaft. Part of the mixer shaft is in the kettle, and the other part is out of the kettle connected with a motor. A heating device is arranged on the outside of the kettle. Firstly, the powder lot and different kinds of liquid are put into the kettle, and then the motor is started, and the mixer shaft and the agitating vane are driven by the motor for mixing the mixture. At the same time, the heating device is started to heat the kettle for dehydrating the mixture inside the kettle. The utility model is the only device to dehydrate and mix the acidic base material, and has the advantages of reducing the tedious equipment during the process of production as before, simplifying the technical process, improving the productive efficiency, and reducing the production cost.
Description
Technical field
The utility model relates to a kind of equipment of production chemical product, particularly a kind of high speed reactor that acid base-material is dewatered, mixes when being used to produce glass cement.
Background technology
Produce acid glass cement, generally all will dewater, mix acid base-material; Reach above-mentioned purpose, original is operating as: at first powder is delivered to cone blender and mixed, and then deliver to oven for drying, mixed by another mixing apparatus again at last.The equipment that above-mentioned production process is used is many, technology is loaded down with trivial details, is unfavorable for reducing production costs.
Summary of the invention
In order to address the above problem, the purpose of this utility model is to provide a kind of highly versatile, easy to operate high speed reactor.
The technical scheme that its technical problem that solves the utility model adopts is: the high speed reactor, it is characterized in that: comprise kettle, shaft and be installed in stirring arm on the shaft, the shaft that stirring arm is installed is positioned at kettle, another part stretches out kettle and connects with motor, and the outside of kettle is provided with heater.
Wherein, described shaft is divided into high-speed stirred axle and stirring at low speed axle, stirring arm on the high-speed stirred axle is divided into butterfly slurry and dispersion impeller, dispersion impeller is installed in the lower end of high-speed stirred axle, the plane and the axes intersect of high-speed stirred axle at butterfly slurry paddle place, the stirring arm on the stirring at low speed axle is that hinged joint is starched.
Wherein, the bottom of described stirring at low speed axle is fixed with bracing frame, is fixed with scraper plate on the bracing frame.
Wherein, described heater comprises chuck, and chuck is wrapped in the outside of kettle, and chuck is provided with fluid inlet and outlet, or designs heating in chuck.
The beneficial effects of the utility model: at first powder, various liquid are added in the kettle, starter motor then, motor will drive shaft and stirring arm, thereby compound is mixed.Simultaneously, open heater, allow heat pass in the kettle, thereby material in the kettle is carried out processed.Depend merely on the utility model and just can dewater, mix, so just can reduce the loaded down with trivial details equipment in the production process in the past, simplify technical process, enhance productivity, reduce production costs acid base-material.
Description of drawings
Below in conjunction with drawings and Examples the utility model is further specified.
Fig. 1 is a structural representation of the present utility model;
Fig. 2 is the structural representation that the stirring at low speed axle is connected with motor;
Fig. 3 is the structural representation that the high-speed stirred axle is connected with motor.
The specific embodiment
Referring to figs. 1 through Fig. 3, the high speed reactor, it comprises kettle 1, shaft and is installed in stirring arm on the shaft, and the shaft that stirring arm is installed is positioned at kettle 1, and another part stretches out kettle 1 and connects with motor 2, and the outside of kettle 1 is provided with heater.At first powder, various liquid are added in the kettle 1, starter motor 2 then, and motor 2 will drive shaft and stirring arm, thereby compound is mixed.Simultaneously, open heater, allow heat pass in the kettle 1, thereby material in the kettle 1 is carried out processed.Depend merely on the utility model and just can dewater, mix, so just can reduce the loaded down with trivial details equipment in the production process in the past, simplify technical process, enhance productivity, reduce production costs acid base-material.
Wherein, described shaft is divided into high-speed stirred axle 3 and stirring at low speed axle 4, stirring arm on the high-speed stirred axle 3 is divided into butterfly slurry 5 and dispersion impeller 6, dispersion impeller 6 is installed in the lower end of high-speed stirred axle 3, the plane and the axes intersect of high-speed stirred axle 3 at butterfly slurry paddle 7 places, the stirring arm on the stirring at low speed axle 4 is that hinged joint starches 8.Butterfly slurry 5, dispersion impeller 6 and hinged joint slurry 8 motion simultaneously make base-material produce turbulent motion in kettle 1, are allowed to condition at abundant mixed dehydration in the kettle 1.High-speed stirred axle 3 connects with motor 2 by soft shaft coupling 14, and mechanically-sealing apparatus 15 is installed on its axis body.Stirring at low speed axle 4 then connects with motor 2 by positive coupling 16, decelerator 17, and its axis body surface is by 18 sealings of V-seal material.
In order to prevent that base-material is bonded at the kettle inboard, the bottom of described stirring at low speed axle 4 is fixed with bracing frame 9, is fixed with scraper plate 10 on the bracing frame 9.When stirring at low speed axle 4 rotated, bracing frame 9, scraper plate 10 will and then rotate, thereby the base-material that will be bonded at kettle 1 inboard strikes off, and prevented to produce at the bottom of still wall and still the phenomenon of high temperature knot charcoal.
Wherein, described heater comprises chuck 11, and chuck 11 is wrapped in the outside of kettle 1, and chuck 11 is provided with fluid inlet 12 and outlet 13.Allow high temperature fluid flow in the chuck 11, allow it just flow out 13 and can heat then, thereby base-material is toasted kettle 1 from exporting from import 12.Certainly, heating 19 also can be set in chuck 11 comes kettle 1 heating.
Certainly, the utility model is not limited to the above embodiments, is equal to the utility model or becomes bad technical scheme also should belong within the protection domain of the present utility model.
Claims (4)
1, high speed reactor, it is characterized in that: comprise kettle (1), shaft and be installed in stirring arm on the shaft, the shaft that stirring arm is installed is positioned at kettle (1), and another part stretches out kettle (1) and connects with motor (2), and the outside of kettle (1) is provided with heater.
2, high speed reactor according to claim 1, it is characterized in that: described shaft is divided into high-speed stirred axle (3) and stirring at low speed axle (4), stirring arm on the high-speed stirred axle (3) is divided into butterfly slurry (5) and dispersion impeller (6), dispersion impeller (6) is installed in the lower end of high-speed stirred axle (3), the plane and the axes intersect of high-speed stirred axle (3) at butterfly slurry paddle (7) place, the stirring arm on the stirring at low speed axle (4) is that hinged joint is starched (8).
3, high speed reactor according to claim 2 is characterized in that: the bottom of described stirring at low speed axle (4) is fixed with bracing frame (9), is fixed with scraper plate (10) on the bracing frame (9).
4, high speed reactor according to claim 1, it is characterized in that: described heater comprises chuck (11), chuck (11) is wrapped in the outside of kettle (1), and chuck (11) is provided with fluid inlet (12) and outlet (13), or designs heating (19) in chuck.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200620063107 CN200939378Y (en) | 2006-08-18 | 2006-08-18 | High speed reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200620063107 CN200939378Y (en) | 2006-08-18 | 2006-08-18 | High speed reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN200939378Y true CN200939378Y (en) | 2007-08-29 |
Family
ID=38745569
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200620063107 Expired - Fee Related CN200939378Y (en) | 2006-08-18 | 2006-08-18 | High speed reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN200939378Y (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101879431A (en) * | 2010-06-29 | 2010-11-10 | 常熟市龙宇化工设备有限公司 | Reaction tank |
| CN103768977A (en) * | 2014-01-23 | 2014-05-07 | 朱其安 | Base material production method and base material machine |
| CN104028138A (en) * | 2014-06-19 | 2014-09-10 | 黎泽荣 | Agitator |
| CN104984708A (en) * | 2015-06-24 | 2015-10-21 | 张家港市顺佳隔热技术有限公司 | High-speed mixing reaction kettle |
| CN108745166A (en) * | 2018-05-23 | 2018-11-06 | 江西省耐力科技股份有限公司 | A kind of lithium battery slurry vacuum stirring device and processing technology |
-
2006
- 2006-08-18 CN CN 200620063107 patent/CN200939378Y/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101879431A (en) * | 2010-06-29 | 2010-11-10 | 常熟市龙宇化工设备有限公司 | Reaction tank |
| CN101879431B (en) * | 2010-06-29 | 2012-09-05 | 常熟市龙宇化工设备有限公司 | Reaction tank |
| CN103768977A (en) * | 2014-01-23 | 2014-05-07 | 朱其安 | Base material production method and base material machine |
| CN104028138A (en) * | 2014-06-19 | 2014-09-10 | 黎泽荣 | Agitator |
| CN104984708A (en) * | 2015-06-24 | 2015-10-21 | 张家港市顺佳隔热技术有限公司 | High-speed mixing reaction kettle |
| CN108745166A (en) * | 2018-05-23 | 2018-11-06 | 江西省耐力科技股份有限公司 | A kind of lithium battery slurry vacuum stirring device and processing technology |
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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: 20070829 Termination date: 20100818 |