CN201669103U - Reactor - Google Patents
Reactor Download PDFInfo
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- CN201669103U CN201669103U CN2010201653375U CN201020165337U CN201669103U CN 201669103 U CN201669103 U CN 201669103U CN 2010201653375 U CN2010201653375 U CN 2010201653375U CN 201020165337 U CN201020165337 U CN 201020165337U CN 201669103 U CN201669103 U CN 201669103U
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- reactor
- axial flow
- kettle
- aerofoil profile
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Abstract
The utility model relates to a reactor belonging to the field of pharmacy machinery industry in order to reduce time spent on extraction and stratifying processes and improve extraction effect. The reactor comprises a mechanical seal device and a wing type axial flow agitator shaft, wherein the mechanical seal device is used at the agitating hole part of a reactor cover for connecting and sealing the reactor cover and the wing type axial flow agitator shaft; the wing type axial flow agitator shaft is arranged at the lower end of the mechanical seal device, and vertically inserted in a reaction space in the reactor through the agitating hole; the lower end of the wing type axial flow agitator shaft is provided with three agitating blades, and the three agitating blades are mutually arranged in a 120-degree angle. In the reactor, the wing type axial flow agitator shaft is matched with enamelled D type deflectors in work, and paddle type agitating blades are replaced by the three agitating blades. Extraction efficiency can be largely improved, material extraction time after reaction is shortened to one half of the original, and meanwhile, extraction effect is largely enhanced.
Description
Technical field
The utility model belongs to the pharmaceutical machine industrial circle, is specifically related to a kind of reactor.
Background technology
Agitator is known as impeller or blade again, and it is the core component of mixing plant.The flow pattern that produces in the stirred tank according to agitator, agitator can be divided into two kinds of axial flow and radial flows basically.For example, pusher impeller, novel aerofoil vane etc. belong to the axial flow agitator, and various straight leaves, curved leaf turbine wheel then belong to the radial flow agitator.
Agitator vertically inserts in the still from the stirred tank top center usually, also adopts the side to insert sometimes, and the bottom is stretched into or mode is stretched in the side.Should require to select different mounting means according to different stirrings.
Be to eliminate the phenomenon of turning round and round of liquid in the stirred vessel, the liquid that is stirred is seethed up and down and reach uniform mixing, need usually add baffle plate in the stirred vessel again.Usually the width of baffle plate is about 1/12～1/10 of container interior diameter, and wherein annex in the equipment such as thermometer or various supporter also can play certain baffle effect, but often do not reach " full baffle plate condition ".Usually increase baffle plate and count its width of meter, power consumption also can increase, but is increased to after the certain value, and power consumption just can not increase again, and the operating mode of this moment just is called " full baffle plate condition ".
In the synthetic medicine company technology of Cefprozil, reactor used in the prior art, usually after finishing, the fluent material reaction needs extracting and demixing, the reactor that is used for extracting and demixing is awl end glassed steel reaction vessels, agitator arm is the slurry formula, as shown in Figure 1, it generally includes cycloidal planetary gear speed reducer 101, frame 102, packing seal 103, clean-out cover 104, thermometer boss 105 and enamel and stirs parts such as paddle agitator 106, after filling with extract in the still, start and stir, rotating speed is 82.5r/min, and after 1 minute, liquid just begins to form the phenomenon of turning round and round.Exist the extraction time long in this scheme implementation process, deficiencies such as effect of extracting difference.
The utility model content
(1) technical problem that will solve
Technical problem to be solved in the utility model is to shorten consumed time in the extracting and demixing process, improves its effect of extracting.
(2) technical scheme
For solving the problems of the technologies described above, the utility model provides a kind of reactor, comprises cylindrical shape kettle, frame, cycloidal planetary gear speed reducer, mechanically-sealing apparatus and aerofoil profile axial flow type stirrer axle; Described kettle upper end is provided with kettle cover, and described kettle cover middle position is provided with poke hole;
Described mechanically-sealing apparatus is arranged at described poke hole place, is used for carrying out at described poke hole place the sealing that is connected between kettle cover and the aerofoil profile axial flow type stirrer axle;
Described aerofoil profile axial flow type stirrer axle is arranged at described mechanically-sealing apparatus lower end, vertically inserts in the described kettle internal-response space from described poke hole, is used for the stirring and the mixing of material;
Described aerofoil profile axial flow type stirrer axle lower end comprises three stirring vanes, and described three blades are 120 degree angles each other and are provided with.
Be provided with described three stirring vanes on three height and positions with the certain altitude interval on the described aerofoil profile axial flow type stirrer axle.
Described reactor also comprises oil-collecting device; Described oil-collecting device is arranged at described mechanically-sealing apparatus lower end, is used to check whether mechanically-sealing apparatus damages.
Described reactor also comprises sleeve pipe stuffing box and enamel D type deflection plate;
Described sleeve pipe stuffing box is arranged on kettle cover one side of described kettle, is used for the sealing between described enamel D type deflection plate and the kettle cover;
Described enamel D type deflection plate vertically inserts in the described kettle internal-response space by described sleeve pipe stuffing box, has been used for baffle effect, and then eliminates the phenomenon of turning round and round of liquid in the whipping process still.
Described enamel D type deflection plate lower end is the D font.
(3) beneficial effect
By using the reactor that technical solutions of the utility model provided, by the work that cooperatively interacts of aerofoil profile axial flow type stirrer axle and enamel D type deflection plate, the materials abstraction time shortens to before half after making reaction finish, and improves the effect of extraction simultaneously greatly.
Description of drawings
Fig. 1 is the panorama sketch of reactor in the prior art
Fig. 2 is the panorama sketch of the reactor that the utility model proposed
The specific embodiment
For making the purpose of this utility model, content and advantage clearer,, the specific embodiment of the present utility model is described in further detail below in conjunction with drawings and Examples.Following examples only are used for the technical solution of the utility model more clearly is described, and can not limit protection domain of the present utility model with this.
Embodiment
Present embodiment specifically describes the architectural feature of the reactor that technical solutions of the utility model provided.
As shown in Figure 2, described reactor comprises:
Cylindrical shape kettle, frame 202, cycloidal planetary gear speed reducer 201, mechanically-sealing apparatus 203, oil-collecting device 204, sleeve pipe stuffing box 205, enamel D type deflection plate 206 and aerofoil profile axial flow type stirrer axle 207;
Described kettle upper end is provided with kettle cover, and described kettle cover middle position is provided with poke hole;
Described frame 202 is cylindrical, supports cycloidal planetary gear speed reducer 201, and the connection space of aerofoil profile axial flow type stirrer axle 207 with cycloidal planetary gear speed reducer 201 is provided, and aerofoil profile axial flow type stirrer axle 207 is supported and locatees;
Described cycloidal planetary gear speed reducer 201, be arranged at described frame 202 upper ends, the lower end extends to described kettle cover poke hole place, and the lower end connects described aerofoil profile axial flow type stirrer axle 207, when being used for reactor worked described aerofoil profile axial flow type stirrer axle 207 is driven and slows down;
Described mechanically-sealing apparatus 203 is arranged at the kettle cover poke hole place of described cycloidal planetary gear speed reducer 201 lower ends, is used for carrying out at described poke hole place the sealing that is connected between kettle cover and the aerofoil profile axial flow type stirrer axle 207;
Described oil-collecting device 204 is arranged at described mechanically-sealing apparatus 203 lower ends, is used to check whether mechanically-sealing apparatus 203 damages;
Described sleeve pipe stuffing box 205 is arranged on kettle cover one side of described kettle, is used for the sealing between described enamel D type deflection plate 206 and the kettle cover;
Described enamel D type deflection plate 206, vertically insert in the described kettle internal-response space by described sleeve pipe stuffing box 205, be used for baffle effect, and then the phenomenon of turning round and round of the interior liquid of elimination whipping process still, count its width of meter because of increasing baffle plate, power consumption also can increase, so its lower end is made into the D type.
Described aerofoil profile axial flow type stirrer axle 207 is arranged at described mechanically-sealing apparatus 203 lower ends, vertically inserts in the kettle internal-response space from described kettle cover poke hole, is used for the stirring and the mixing of material.
Described aerofoil profile axial flow type stirrer axle 207 lower ends comprise three stirring vanes, and described three blades are 120 degree angles each other and are provided with.
Be provided with described three stirring vanes on three height and positions with the certain altitude interval on the described aerofoil profile axial flow type stirrer axle 207.
The workflow of this reactor is:
The filling extract starts the reactor stirring motor in the reactor, and the driven by motor reductor drops to 125r/min with rotating speed by 1450r/min, and after 10 seconds, extract begins to roll up and down, and the extraction time is short, the efficient height.
By using the reactor that technical solutions of the utility model provided, by the work that cooperatively interacts of aerofoil profile axial flow type stirrer axle and enamel D type deflection plate, the three-chip type stirring vane contrasts enamel of the prior art and starches the formula stirring vane.Can improve extraction efficiency greatly, make the reaction end back materials abstraction time shorten to before half, also improve the effect of extraction simultaneously greatly.
The above only is a preferred implementation of the present utility model; should be understood that; for those skilled in the art; under the prerequisite that does not break away from the utility model know-why; can also make some improvement and distortion, these improvement and distortion also should be considered as protection domain of the present utility model.
Claims (5)
1. reactor, comprise cylindrical shape kettle, frame and cycloidal planetary gear speed reducer, described kettle upper end is provided with kettle cover, and described kettle cover middle position is provided with poke hole, it is characterized in that described reactor also comprises mechanically-sealing apparatus and aerofoil profile axial flow type stirrer axle;
Described mechanically-sealing apparatus is arranged at described poke hole place, is used for carrying out at described poke hole place the sealing that is connected between kettle cover and the aerofoil profile axial flow type stirrer axle;
Described aerofoil profile axial flow type stirrer axle is arranged at described mechanically-sealing apparatus lower end, vertically inserts in the described kettle internal-response space from described poke hole, is used for the stirring and the mixing of material;
Described aerofoil profile axial flow type stirrer axle lower end comprises three stirring vanes, and described three blades are 120 degree angles each other and are provided with.
2. reactor as claimed in claim 1 is characterized in that, is provided with described three stirring vanes on three height and positions with the certain altitude interval on the described aerofoil profile axial flow type stirrer axle.
3. reactor as claimed in claim 1 is characterized in that described reactor also comprises oil-collecting device; Described oil-collecting device is arranged at described mechanically-sealing apparatus lower end, is used to check whether mechanically-sealing apparatus damages.
4. reactor as claimed in claim 1 is characterized in that, described reactor also comprises sleeve pipe stuffing box and enamel D type deflection plate;
Described sleeve pipe stuffing box is arranged on kettle cover one side of described kettle, is used for the sealing between described enamel D type deflection plate and the kettle cover;
Described enamel D type deflection plate vertically inserts in the described kettle internal-response space by described sleeve pipe stuffing box, has been used for baffle effect, and then eliminates the phenomenon of turning round and round of liquid in the whipping process still.
5. reactor as claimed in claim 4 is characterized in that, described enamel D type deflection plate lower end is the D font.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010201653375U CN201669103U (en) | 2010-04-20 | 2010-04-20 | Reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010201653375U CN201669103U (en) | 2010-04-20 | 2010-04-20 | Reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201669103U true CN201669103U (en) | 2010-12-15 |
Family
ID=43326516
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010201653375U Expired - Fee Related CN201669103U (en) | 2010-04-20 | 2010-04-20 | Reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201669103U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102784613A (en) * | 2012-09-05 | 2012-11-21 | 南京工业大学 | Stirring reaction device for synthesizing super absorbent resin |
| CN103863724A (en) * | 2014-03-12 | 2014-06-18 | 临沂宏业化工设备有限公司 | Enameled glass vessel and base coat formula thereof |
| CN105273845A (en) * | 2014-07-16 | 2016-01-27 | 上海禾汽玻璃仪器有限公司 | Rose oil distillation purification unit |
-
2010
- 2010-04-20 CN CN2010201653375U patent/CN201669103U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102784613A (en) * | 2012-09-05 | 2012-11-21 | 南京工业大学 | Stirring reaction device for synthesizing super absorbent resin |
| CN102784613B (en) * | 2012-09-05 | 2014-05-14 | 南京工业大学 | Stirring reaction device for synthesizing super absorbent resin |
| CN103863724A (en) * | 2014-03-12 | 2014-06-18 | 临沂宏业化工设备有限公司 | Enameled glass vessel and base coat formula thereof |
| CN103863724B (en) * | 2014-03-12 | 2016-03-16 | 临沂宏业化工设备有限公司 | A kind of anticorrosion enamelled vessel |
| CN105273845A (en) * | 2014-07-16 | 2016-01-27 | 上海禾汽玻璃仪器有限公司 | Rose oil distillation purification unit |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| 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: 20101215 Termination date: 20190420 |