CN213193690U - Addition reaction kettle for high-viscosity organic silicone oil - Google Patents
Addition reaction kettle for high-viscosity organic silicone oil Download PDFInfo
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- CN213193690U CN213193690U CN202021847884.1U CN202021847884U CN213193690U CN 213193690 U CN213193690 U CN 213193690U CN 202021847884 U CN202021847884 U CN 202021847884U CN 213193690 U CN213193690 U CN 213193690U
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Abstract
The utility model relates to the technical field of silicone oil reaction kettles, in particular to an addition reaction kettle for high-viscosity organic silicone oil, wherein an observation window is embedded in the front of a main body, a bracket is welded on the outer side of the main body, a support rod is welded on the bottom of the main body, a top cover is fixedly connected on the top of the main body through a screw, a connector is arranged on the top of the top cover, a speed reducer is arranged at the center of the top cover, a motor is arranged right above the speed reducer, the output end of the motor is rotatably connected with a crankshaft, a stirring rod and a first stirring blade are respectively clamped on the outer side of the crankshaft, a stirring plate and a second stirring blade are respectively welded on the outer side of the stirring rod, and a through hole is penetrated through the top, the problems of poor quality and poor quality of silicone oil addition caused by the fact that the proportioned silicone oil is not uniform enough and the stirring effect is not good enough are solved.
Description
Technical Field
The utility model relates to a silicon oil reation kettle technical field, in particular to addition reation kettle of high viscous silicone oil.
Background
The broad understanding of the reaction kettle is that the reaction kettle is a container for physical or chemical reaction, the heating, evaporation, cooling and low-speed and high-speed mixing functions required by the process are realized by the structural design and parameter configuration of the container, the reaction kettle is widely applied to pressure containers for petroleum, chemical engineering, rubber, pesticides, dyes, medicines and foods and used for completing the processes of vulcanization, nitration, hydrogenation, alkylation, polymerization, condensation and the like, and the high-viscosity organic silicon oil needs to be added into an addition reaction kettle of the high-viscosity organic silicon oil during addition.
However, the existing addition reaction kettle for high-viscosity organic silicone oil has poor extrusion stirring effect on proportioned silicone oil when in use, so that the proportioned silicone oil is not uniform enough and the stirring effect is not good enough, thereby causing the problem of poor quality and quality of silicone oil addition.
SUMMERY OF THE UTILITY MODEL
The utility model aims to provide an addition reation kettle of high viscous silicone oil to prior art's defect and not enough.
In order to achieve the above object, the utility model adopts the following technical scheme:
a high silicone oil's addition reation kettle, it includes the main part, the front embedding of main part has the observation window, the outside welding of main part has the support, the bottom welding of main part has the bracing piece, screw fixedly connected with top cap is passed through at the top of main part, the interface has been seted up at the top of top cap, the center department at top cap top installs the speed reducer, install the motor directly over the speed reducer, the output of motor rotates and is connected with the spindle, the outside of spindle is the joint respectively has puddler and first stirring leaf, stirring board and second stirring leaf have been welded respectively in the outside of puddler, the top of stirring board is run through there is the through-hole.
Further, the inner wall of main part is provided with the screw thread draw-in groove, the main part be "cylindrical".
Further, the stirring board is provided with four, four the stirring board equidistance is arranged, stirring board and second stirring leaf and puddler welded connection.
Furthermore, the through holes are equal in size and penetrate through the top of the stirring plate irregularly.
Furthermore, the interface is provided with a plurality of, a plurality of the interface size shape is different.
Further, the outer diameter of the machine shaft is matched with the inner diameter of the stirring rod, threads are arranged on the outer side of the machine shaft, and the machine shaft is rotatably connected with the stirring rod through the threads.
After the structure is adopted, the utility model discloses beneficial effect does: the utility model discloses a stirring board and puddler and stirring leaf that set up, when using, the staff first for equipment switch on, then the interface on the top cap switches on the equipment that reation kettle needs to use such as condenser and vacuum apparatus, the staff adds the silicone oil material of ratio through the interface afterwards, make the silicone oil material of ratio flow into in the main part well, the staff starts motor and speed reducer afterwards, make the motor drive the spindle rotation of output, thereby make the spindle drive the puddler and the first stirring leaf that are located the main part inside spindle outside rotate, and the spindle is located the main part inside section and is provided with the screw thread, and the main part inner wall is provided with the screw thread, when making the spindle rotate and drive puddler and the second stirring leaf and the stirring board outside the puddler to rotate, the puddler will be in the screw thread displacement outside the spindle, and the stirring board outside the puddler will be along with the puddler position laminating main part inner wall displacement, make the inside well proportioned silicone oil material of main part extrude and flow out and be stirred by the second stirring leaf in the through-hole on the stirring board by stirring board downward displacement, and the silicone oil on the stirring board will be promoted and from the through-hole internal flow on the stirring board by the stirring of second stirring leaf and the main part bottom and the first stirring leaf stirring in the spindle outside that is located the main part bottom by the spindle when stirring board upward displacement, can extrude the stirring to well proportioned silicone oil like this, make the well proportioned silicone oil stirring more even and stirring effect better, improve the quality and the quality of silicone oil addition effectively.
Drawings
Fig. 1 is a schematic structural diagram of the present invention;
FIG. 2 is a structural cross-sectional view of the body;
FIG. 3 is a partial structural view of the agitating plate.
Description of reference numerals: 1. a motor; 2. a crankshaft; 201. a stirring plate; 202. a first stirring blade; 203. a stirring rod; 204. a through hole; 205. a second stirring blade; 3. a speed reducer; 4. an interface; 5. a top cover; 6. a main body; 601. a support; 7. an observation window; 8. a support rod.
Detailed Description
The present invention will be further described with reference to the accompanying drawings.
As shown in fig. 1 to 3, a high viscosity silicone oil's addition reation kettle, it includes main part 6, the front embedding of main part 6 has observation window 7, the outside welding of main part 6 has support 601, the bottom welding of main part 6 has bracing piece 8, screw fixedly connected with top cap 5 is passed through at the top of main part 6, interface 4 has been seted up at the top of top cap 5, speed reducer 3 is installed to the center department at top cap 5 top, install motor 1 directly over speed reducer 3, the output of motor 1 rotates and is connected with spindle 2, spindle 2's the outside is the joint respectively has puddler 203 and first stirring leaf 202, stirring board 201 and second stirring leaf 205 have been welded respectively in the outside of puddler 203, the top of stirring board 201 runs through there is the through-hole 204.
As the utility model discloses an optimal mode, the inner wall of main part 6 is provided with the thread draw-in groove, and main part 6 is "cylindrical", makes spindle 2 rotate and drives second stirring leaf 205 and the stirring board 201 in the puddler 203 and the puddler 203 outside and rotate, and the puddler 203 will carry out the displacement along the screw thread in the spindle 2 outside, and the stirring board 201 in the puddler 203 outside will carry out the displacement along with puddler 203 position laminating main part 6 inner walls, thereby realizes that puddler 203 drives stirring board 201 displacement from top to bottom.
As a preferred mode of the utility model, stirring board 201 is provided with four, four stirring board 201 equidistance are arranged, stirring board 201 and second stirring leaf 205 and puddler 203 welded connection, the stirring board 201 in the puddler 203 outside will be along with puddler 203 position laminating main part 6 inner wall carry out the displacement, make the inside silicon oil material that matches of main part 6 extrude and flow out and be stirred by second stirring leaf 205 in the through-hole 204 on the stirring board 201 when being stirred board 201 downward displacement, improve the stirring effect.
As an optimized mode of the utility model, the through-hole 204 size equals, through-hole 204 is irregular to run through in the top of stirring board 201, the stirring board 201 in the stirring rod 203 outside carries out the displacement along with stirring rod 203 position laminating main part 6 inner wall, make the inside silicon oil material that matches of main part 6 extrude and flow out in the through-hole 204 on the stirring board 201 and stir by second stirring leaf 205 when being stirred board 201 downward displacement, stirring board 201 in the stirring rod 203 outside will be along with stirring rod 203 position laminating main part 6 inner wall and carry out the displacement, make the inside silicon oil material that matches of main part 6 extrude and flow out and stir by second stirring leaf 205 in the through-hole 204 on the stirring board 201 when being stirred board 201 downward displacement, thereby make the stirring effect better.
As an optimized mode of the utility model, interface 4 is equipped with a plurality ofly, and the 4 big or small shapes of a plurality of interfaces are different, and interface 4 on top cap 5 switches on the equipment that reation kettle need use like condenser and vacuum vessel etc for reation kettle can normally work.
As the utility model discloses an optimal mode, the external diameter of spindle 2 and the internal diameter looks adaptation of puddler 203, spindle 2's the outside is provided with the screw thread, spindle 2 rotates with puddler 203 through the screw thread to be connected, when making spindle 2 rotate the second stirring leaf 205 and the stirring board 201 that drive the puddler 203 and the puddler 203 outside and rotate, puddler 203 will carry out the displacement at the screw thread in the spindle 2 outside, can extrude the stirring to the silicon oil that the ratio is good like this, make the more even and stirring effect of the silicon oil stirring that the ratio is good better, improve the quality and the quality of silicon oil addition effectively.
The working principle is as follows: when the reactor is used, a worker firstly switches on a power supply for the equipment, then the interface 4 on the top cover 5 switches on the equipment needed by the reactor, such as a condenser, a vacuum and the like, and then the worker adds proportioned silicone oil material through the interface 4, so that the proportioned silicone oil material flows into the main body 6, then the worker starts the motor 1 and the speed reducer 3, so that the motor 1 drives the shaft 2 at the output end to rotate, so that the shaft 2 drives the stirring rod 203 and the first stirring blade 202 which are positioned at the outer side of the shaft 2 inside the main body 6 to rotate, the section of the shaft 2 which is positioned inside the main body 6 is provided with threads, and the inner wall of the main body 6 is provided with threads, so that when the shaft 2 rotates to drive the stirring rod 203 and the second stirring blade 205 and the stirring plate 201 which are positioned at the outer side of the stirring rod 203 to rotate, the stirring rod 203 can displace along with the threads at the outer side of the shaft 2, make the inside well proportioned silicone oil material of main part 6 extrude and flow out in the through-hole 204 on the stirring board 201 and be stirred by second stirring leaf 205 when being stirred board 201 downward displacement, and the silicone oil on the stirring board 201 will be stirred by second stirring leaf 205 and promote and flow down main part 6 bottom and be stirred by the first stirring leaf 202 in the spindle 2 outside that spindle 2 is located the main part 6 bottom in through-hole 204 on the stirring board 201 when stirring board 201 upward displacement, can extrude the stirring to well proportioned silicone oil like this, make the more even and stirring effect of well proportioned silicone oil stirring better, improve the quality and the quality of silicone oil addition effectively.
The above is only the preferred embodiment of the present invention, so all the equivalent changes or modifications made by the structure, features and principles in accordance with the claims of the present invention are included in the claims of the present invention.
Claims (6)
1. The addition reaction kettle for the high-viscosity organic silicone oil comprises a main body (6) and is characterized in that: the front embedding of main part (6) has observation window (7), the outside welding of main part (6) has support (601), the bottom welding of main part (6) has bracing piece (8), screw fixedly connected with top cap (5) are passed through at the top of main part (6), interface (4) have been seted up at the top of top cap (5), the center department at top cap (5) top installs speed reducer (3), install motor (1) directly over speed reducer (3), the output of motor (1) rotates and is connected with spindle (2), the outside of spindle (2) is the joint respectively has puddler (203) and first stirring leaf (202), stirring board (201) and second stirring leaf (205) have been welded respectively in the outside of puddler (203), the top of stirring board (201) is run through there is through-hole (204).
2. The addition reaction kettle for high-viscosity silicone oil according to claim 1, characterized in that: the inner wall of main part (6) is provided with the screw thread draw-in groove, main part (6) be "cylindrical".
3. The addition reaction kettle for high-viscosity silicone oil according to claim 1, characterized in that: stirring board (201) are provided with four, four stirring board (201) equidistance is arranged, stirring board (201) and second stirring leaf (205) and puddler (203) welded connection.
4. The addition reaction kettle for high-viscosity silicone oil according to claim 1, characterized in that: the through holes (204) are equal in size, and the through holes (204) irregularly penetrate through the top of the stirring plate (201).
5. The addition reaction kettle for high-viscosity silicone oil according to claim 1, characterized in that: the connector (4) is provided with a plurality of connectors, and the connectors (4) are different in size and shape.
6. The addition reaction kettle for high-viscosity silicone oil according to claim 1, characterized in that: the outer diameter of the crankshaft (2) is matched with the inner diameter of the stirring rod (203), threads are arranged on the outer side of the crankshaft (2), and the crankshaft (2) is rotatably connected with the stirring rod (203) through the threads.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202021847884.1U CN213193690U (en) | 2020-08-31 | 2020-08-31 | Addition reaction kettle for high-viscosity organic silicone oil |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202021847884.1U CN213193690U (en) | 2020-08-31 | 2020-08-31 | Addition reaction kettle for high-viscosity organic silicone oil |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN213193690U true CN213193690U (en) | 2021-05-14 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202021847884.1U Active CN213193690U (en) | 2020-08-31 | 2020-08-31 | Addition reaction kettle for high-viscosity organic silicone oil |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN213193690U (en) |
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- 2020-08-31 CN CN202021847884.1U patent/CN213193690U/en active Active
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Address after: 515098 No.1 Zhiye Road, nanshanwan Industrial Park, Binhai street, Haojiang District, Shantou City, Guangdong Province Patentee after: Guangdong Tuoxin Organic Silicon Technology Co.,Ltd. Address before: 515098 No.1 Zhiye Road, nanshanwan Industrial Park, Binhai street, Haojiang District, Shantou City, Guangdong Province Patentee before: Shantou Tuoxin silicone Technology Co.,Ltd. |