CN220610383U - Modified silica gel reaction kettle capable of circulating materials up and down - Google Patents
Modified silica gel reaction kettle capable of circulating materials up and down Download PDFInfo
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- CN220610383U CN220610383U CN202322225223.5U CN202322225223U CN220610383U CN 220610383 U CN220610383 U CN 220610383U CN 202322225223 U CN202322225223 U CN 202322225223U CN 220610383 U CN220610383 U CN 220610383U
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- 239000000463 material Substances 0.000 title claims abstract description 71
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical class O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 title claims abstract description 70
- 238000006243 chemical reaction Methods 0.000 title claims abstract description 29
- 238000012545 processing Methods 0.000 claims abstract description 23
- 238000003756 stirring Methods 0.000 claims description 49
- 238000010008 shearing Methods 0.000 claims description 35
- 230000005540 biological transmission Effects 0.000 claims description 27
- 238000007790 scraping Methods 0.000 claims description 22
- 239000006185 dispersion Substances 0.000 claims description 20
- 238000003754 machining Methods 0.000 claims description 5
- 239000000741 silica gel Substances 0.000 abstract description 5
- 229910002027 silica gel Inorganic materials 0.000 abstract description 5
- 238000000034 method Methods 0.000 description 8
- 230000008569 process Effects 0.000 description 8
- 230000000694 effects Effects 0.000 description 5
- 238000004519 manufacturing process Methods 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 2
- 230000009471 action Effects 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 229940079593 drug Drugs 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 239000000975 dye Substances 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 238000005984 hydrogenation reaction Methods 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 230000033001 locomotion Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000006396 nitration reaction Methods 0.000 description 1
- 239000000575 pesticide Substances 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 239000005060 rubber Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000007306 turnover Effects 0.000 description 1
- 238000004073 vulcanization Methods 0.000 description 1
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- Mixers Of The Rotary Stirring Type (AREA)
Abstract
The utility model belongs to the technical field of silica gel processing equipment, and particularly relates to a modified silica gel reaction kettle capable of circulating materials up and down.
Description
Technical Field
The utility model belongs to the technical field of silica gel processing equipment, and particularly relates to a modified silica gel reaction kettle for circulating materials up and down.
Background
The reaction kettle is widely understood to be a container with physical or chemical reaction, and through structural design and parameter configuration of the container, the heating, evaporating, cooling and low-speed mixing functions of technological requirements are realized, and the reaction kettle is widely applied to petroleum, chemical industry, rubber, pesticides, dyes, medicines and foods, and is used for completing the technological processes of vulcanization, nitration, hydrogenation, hydrocarbylation, polymerization, condensation and the like.
In the production and preparation process of silica gel, a silica gel reaction kettle is an indispensable device. The silica gel reaction kettle mainly comprises a reaction container, a stirring device, a heating device, a bracket and other structures, wherein after materials are added into the reaction container, the stirring device is started, and the materials are stirred and mixed under the action of a stirring paddle.
The stirring device of the existing reaction kettle comprises a stirring shaft and a stirring paddle arranged on the stirring shaft, wherein the stirring paddle is fixedly arranged. When the materials are stirred, the stirring paddles can fully stir the materials on the circumference of the stirring paddles, but the stirring conditions of the materials above and below the stirring paddles are not ideal, so that the uniformity of the overall stirring of the materials is not ideal, and the quality of products is affected.
Disclosure of Invention
The utility model aims to provide a modified silica gel reaction kettle capable of circulating materials up and down, and aims to solve the technical problems that in the prior art, the stirring condition of the reaction kettle on materials above and below a stirring paddle is not ideal, and the uniformity of the overall stirring of the materials is not ideal.
In order to achieve the above object, the embodiment of the utility model provides a modified silica gel reaction kettle for circulating materials up and down, comprising:
machining a support;
the kettle body is arranged in the processing support, and the inside of the kettle body is hollow for storing modified silica gel materials;
the revolution main shaft part is rotatably arranged on the processing support and driven by a first power part;
the rotating outer sleeve is rotatably arranged on the revolution main shaft piece and driven by a second power piece;
the dispersing and shearing shaft is rotatably arranged at the bottom of the revolution main shaft piece and is accommodated in the kettle body, and the dispersing and shearing shaft and the revolution main shaft piece are in meshed transmission for shearing the modified silica gel material;
the double-paddle turning shaft is rotatably arranged at the bottom of the revolution main shaft piece and is accommodated in the kettle body, and the double-paddle turning shaft and the autorotation outer sleeve are in meshed transmission for turning up the modified silica gel material;
and the anti-sticking wall scraping knife is fixedly arranged at the bottom of the revolution main shaft part and is accommodated in the kettle body, wherein the anti-sticking wall scraping knife is contacted with the inner wall of the kettle body so as to scrape off the modified silica gel material on the inner wall of the kettle body.
Optionally, the dispersing and shearing shaft comprises a first rotating shaft, an upper butterfly stirrer, an upper dispersing disc, a lower butterfly stirrer and a lower dispersing disc; the first rotating shaft is rotatably arranged at the bottom of the revolution main shaft piece and is accommodated in the kettle body, and the first rotating shaft and the revolution main shaft piece are in meshed transmission; the upper butterfly stirrer, the upper dispersing disc, the lower butterfly stirrer and the lower dispersing disc are sequentially arranged at intervals from top to bottom along the length direction of the first rotating shaft.
Optionally, the inclination direction of the stirring sheet on the upper butterfly stirrer is opposite to the inclination direction of the stirring sheet on the lower butterfly stirrer; when the stirring sheet on the upper butterfly stirrer inclines leftwards, the first rotating shaft rotates clockwise; when the upper stirring blade of the upper butterfly stirrer inclines rightwards, the first rotating shaft rotates anticlockwise; so that the upper butterfly stirrer presses down the modified silica gel material, and the lower butterfly stirrer turns up the modified silica gel material.
Optionally, the stirring blade on the upper butterfly stirrer is inclined 45 ° to the left, and the stirring blade on the lower butterfly stirrer is inclined 45 ° to the right.
Optionally, two double-paddle turning shafts are arranged; the dispersing shearing shaft and the anti-sticking wall scraping knife are arranged on the bottom middle line of the revolution main shaft, and the two double-paddle turning shafts are symmetrically arranged on two sides of the bottom middle line of the revolution main shaft.
Optionally, the two double-oar turning shafts have the same structure and comprise a second rotating shaft, a first side turning oar, a second side turning oar and an upward turning pushing blade; the second rotating shaft is rotatably arranged at the bottom of the revolution main shaft piece and is accommodated in the kettle body, and the second rotating shaft and the rotation outer sleeve are in meshed transmission; the first side turning paddles and the second side turning paddles are symmetrically fixed on the left side and the right side of the second rotating shaft; the upward turning pushing blades are sequentially arranged at intervals from top to bottom along the length direction of the second rotating shaft and are distributed in an arc line, and the upward turning pushing blades are connected to the second rotating shaft in a downward inclined mode.
Optionally, a first belt pulley is arranged at the top end of the revolution main shaft member, a second belt pulley is arranged on the output shaft of the first power member, and the first belt pulley and the second belt pulley are connected through a transmission belt; the bottom of revolution main shaft spare is provided with first meshing gear, the top of dispersion shearing axle is provided with the second meshing gear, first meshing gear with the meshing of second meshing gear is transmitted.
Optionally, a first sprocket is arranged at the top end of the self-rotating outer sleeve, a second sprocket is arranged on the output shaft of the second power piece, and the first sprocket and the second sprocket are connected through a transmission chain; the bottom of the self-rotating outer sleeve is provided with a third meshing gear, the top of the double-paddle turning shaft is provided with a fourth meshing gear, and the third meshing gear and the fourth meshing gear are in meshing transmission.
Optionally, the processing support comprises a placement base and a processing base; the kettle body is placed in the placement base, and the revolution main shaft piece, the first power piece and the second power piece are installed on the processing base; the processing base station is connected with the placement base station in a sliding manner, namely, the processing base station moves along the height direction of the placement base station so as to drive the revolution main shaft piece, the dispersion shearing shaft, the double-paddle turning shaft and the anti-sticking scraping wall knife to be close to or far away from the kettle body.
The technical scheme of the modified silica gel reaction kettle for circulating materials up and down provided by the embodiment of the utility model has at least one of the following technical effects: when the modified silica gel reaction kettle for circulating materials up and down works, on one hand, a revolution main shaft part is driven by a first power part to revolve in the kettle body with a dispersion shearing shaft, a double-paddle turning shaft and an anti-sticking wall scraping knife, and meanwhile, the dispersion shearing shaft and the revolution main shaft part are used for meshed transmission, so that the revolution main shaft part drives the dispersion shearing shaft to synchronously rotate on the revolution main shaft part; on the other hand, the second power piece drives the rotation outer sleeve to rotate on the revolution main shaft piece, and meanwhile, the double-paddle turning shaft and the rotation outer sleeve are meshed for transmission, so that the rotation outer sleeve drives the double-paddle turning shaft to synchronously rotate on the revolution main shaft piece. Therefore, the dispersing shearing shaft and the double-paddle turning shaft can revolve along with the revolution main shaft, the stirring area is increased, the stirring efficiency is improved, the modified silica gel materials can be quickly and uniformly mixed together, the double-paddle turning shaft turns the modified silica gel materials at the lower part of the kettle body upwards to the upper part of the kettle body in the rotation process, the circulation of the upper and lower modified silica gel materials in the kettle body is realized, the mixing effect is obviously improved, and the modified silica gel materials on the inner wall of the kettle body are scraped by the anti-sticking scraping knife, so that the modified silica gel materials are stirred more finely and thoroughly, and the stirring is fully and uniformly.
Drawings
In order to more clearly illustrate the technical solutions of the embodiments of the present utility model, the drawings that are needed in the embodiments or the description of the prior art will be briefly described below, it being obvious that the drawings in the following description are only some embodiments of the present utility model, and that other drawings may be obtained according to these drawings without inventive effort for a person skilled in the art.
FIG. 1 is a perspective view of a modified silica gel reaction kettle for circulating materials up and down;
FIG. 2 is a perspective view of the modified silica gel reaction kettle with upper and lower circulating materials provided by the utility model after the kettle body is hidden;
fig. 3 is a schematic structural connection diagram of a revolution main shaft member, a rotation outer sleeve, a dispersion shearing shaft, a double-paddle turning shaft and an anti-sticking wall scraping knife provided by the utility model;
fig. 4 is a bottom view of the revolution main shaft, the rotation outer sleeve, the dispersion shearing shaft, the double-paddle turning shaft and the anti-sticking wall scraping knife provided by the utility model;
FIG. 5 is a schematic view of a dispersive shear shaft according to the present utility model;
fig. 6 is a schematic structural view of a dual-paddle turning shaft provided by the utility model.
Wherein, each reference sign in the figure:
100. machining a support; 110. a base station is arranged; 120. a processing base;
200. a kettle body;
300. a revolution main shaft member; 310. a first pulley; 320. a first meshing gear;
400. a first power member; 410. a second pulley;
500. rotating the outer sleeve; 510. A first sprocket; 520. A third meshing gear;
600. a second power member; 610. A second sprocket;
700. a dispersion shear shaft; 710. A first rotating shaft; 720. An upper butterfly stirrer; 730. a top dispersion plate; 740. A lower butterfly stirrer; 750. A lower dispersion plate; 760. A second meshing gear;
800. double-oar turning shafts; 810. A second rotating shaft; 820. A first side turning paddle; 830. A second side turning paddle; 840. Turning up the pushing blade; 850. A fourth meshing gear;
900. anti-sticking wall scraping knife.
Detailed Description
Embodiments of the present utility model are described in detail below, examples of which are illustrated in the accompanying drawings, wherein like or similar reference numerals refer to like or similar elements or elements having like or similar functions throughout. The embodiments described below by referring to the drawings are exemplary and intended to illustrate embodiments of the utility model and should not be construed as limiting the utility model.
In the description of the embodiments of the present utility model, it should be understood that the terms "length," "width," "upper," "lower," "front," "rear," "left," "right," "vertical," "horizontal," "top," "bottom," "inner," "outer," and the like indicate orientations or positional relationships based on the orientation or positional relationships shown in the drawings, merely to facilitate description of the embodiments of the present utility model and simplify description, and do not indicate or imply that the devices or elements referred to must have a specific orientation, be configured and operated in a specific orientation, and thus should not be construed as limiting the present utility model.
Furthermore, the terms "first," "second," and the like, are used for descriptive purposes only and are not to be construed as indicating or implying a relative importance or implicitly indicating the number of technical features indicated. Thus, a feature defining "a first" or "a second" may explicitly or implicitly include one or more such feature. In the description of the embodiments of the present utility model, the meaning of "plurality" is two or more, unless explicitly defined otherwise.
In the embodiments of the present utility model, unless explicitly specified and limited otherwise, the terms "mounted," "connected," "secured" and the like are to be construed broadly and include, for example, either permanently connected, removably connected, or integrally formed; can be mechanically or electrically connected; can be directly connected or indirectly connected through an intermediate medium, and can be communicated with the inside of two elements or the interaction relationship of the two elements. The specific meaning of the above terms in the embodiments of the present utility model will be understood by those of ordinary skill in the art according to specific circumstances.
In a first embodiment of the present utility model, as shown in fig. 1 to 3, a modified silica gel reaction kettle for circulating materials up and down is provided, comprising:
machining the support 100;
the kettle body 200 is placed in the processing support 100, and the kettle body 200 is hollow in order to store modified silica gel materials;
a revolution main shaft 300, wherein the revolution main shaft 300 is rotatably installed on the machining supporter 100 and driven by a first power member 400;
the rotation outer sleeve 500, the rotation outer sleeve 500 is rotatably installed on the revolution main shaft 300 and driven by a second power member 600;
the dispersing and shearing shaft 700 is rotatably installed at the bottom of the revolution main shaft 300 and is accommodated in the kettle body 200, wherein the dispersing and shearing shaft 700 and the revolution main shaft 300 are in meshed transmission for shearing the modified silica gel material;
the double-paddle turning shaft 800 is rotatably installed at the bottom of the revolution main shaft 300 and is accommodated in the kettle body 200, wherein the double-paddle turning shaft 800 and the rotation outer sleeve 500 are in meshed transmission for turning up the modified silica gel material;
and the anti-sticking wall scraping knife 900 is fixedly arranged at the bottom of the revolution main shaft 300 and is accommodated in the kettle body 200, wherein the anti-sticking wall scraping knife 900 is contacted with the inner wall of the kettle body 200 so as to scrape off the modified silica gel material on the inner wall of the kettle body 200.
Specifically, in this embodiment, when the modified silica gel reaction kettle for circulating materials up and down works, on one hand, the first power member 400 drives the revolution main shaft 300 to carry the dispersion shearing shaft 700, the double-paddle turning shaft 800 and the anti-sticking wall scraping knife 900 to revolve inside the kettle body 200, and meanwhile, the dispersion shearing shaft 700 and the revolution main shaft 300 are engaged and driven, so that the revolution main shaft 300 drives the dispersion shearing shaft 700 to synchronously rotate on the revolution main shaft 300; on the other hand, the second power member 600 drives the rotation outer sleeve 500 to rotate on the revolution main shaft 300, and simultaneously, the double-paddle turning shaft 800 is driven to synchronously rotate on the revolution main shaft 300 by the rotation outer sleeve 500 through meshing transmission between the double-paddle turning shaft 800 and the rotation outer sleeve 500.
Therefore, the dispersing shear shaft 700 and the double-paddle turning shaft 800 in the utility model can revolve along with the revolution main shaft 300 and can rotate, so that the stirring area is increased, the stirring efficiency is improved, the modified silica gel materials can be quickly and uniformly mixed together, the double-paddle turning shaft 800 turns the modified silica gel materials at the lower part of the kettle body 200 upwards to the upper part of the kettle body 200 in the rotation process, the circulation of the upper and lower modified silica gel materials in the kettle body 200 is realized, the mixing effect is obviously improved, and the modified silica gel materials on the inner wall of the kettle body 200 are scraped by the anti-sticking wall scraping knife 900, so that the modified silica gel materials are stirred more finely and thoroughly, and the stirring is fully and uniformly.
In the second embodiment of the present utility model, as shown in fig. 5, the dispersing shear shaft 700 includes a first rotating shaft 710, an upper butterfly stirrer 720, an upper dispersing disc 730, a lower butterfly stirrer 740 and a lower dispersing disc 750; the first rotating shaft 710 is rotatably installed at the bottom of the revolution main shaft 300 and is accommodated in the kettle body 200, and the first rotating shaft 710 and the revolution main shaft 300 are in meshed transmission; the upper butterfly stirrer 720, the upper dispersing disc 730, the lower butterfly stirrer 740 and the lower dispersing disc 750 are sequentially arranged at intervals from top to bottom along the length direction of the first rotating shaft 710.
Specifically, in this embodiment, during the stirring production process of the modified silica gel material, the upper dispersing disc 730 and the lower dispersing disc 750 on the dispersing and shearing shaft 700 rotate along with the first rotating shaft 710 at a high speed, and the modified silica gel material can be effectively dispersed and sheared by the upper dispersing disc 730 and the lower dispersing disc 750, so that the modified silica gel material inside the kettle body 200 can be quickly and mutually infiltrated and uniformly mixed. And an upper butterfly stirrer 720 and a lower butterfly stirrer 740 are additionally arranged on the dispersing and shearing shaft 700, the upper butterfly stirrer 720 and the lower butterfly stirrer 740 rotate along with the first rotating shaft 710 at a high speed, and the upper butterfly stirrer 720 and the lower butterfly stirrer 740 can turn over the modified silica gel materials in the shearing process of the upper dispersing disc 730 and the lower dispersing disc 750, so that the dispersing and shearing effects of the upper dispersing disc 730 and the lower dispersing disc 750 are improved.
The rest of the present embodiment is the same as the first embodiment, and the unexplained features in the present embodiment are all explained by the first embodiment, and are not described here again.
In the third embodiment of the present utility model, as shown in fig. 5, the inclination direction of the stirring blade on the upper butterfly stirrer 720 is opposite to the inclination direction of the stirring blade on the lower butterfly stirrer 740; when the stirring blade on the upper butterfly stirrer 720 is inclined to the left, the first rotation shaft 710 is rotated clockwise; when the upper stirring blade of the upper butterfly stirrer 720 is inclined rightward, the first rotation shaft 710 is rotated counterclockwise; so that the upper butterfly stirrer 720 presses down the modified silica gel material, and the lower butterfly stirrer 740 turns up the modified silica gel material.
Specifically, in this embodiment, the inclination direction of the stirring sheet on the upper butterfly stirrer 720 is opposite to the inclination direction of the stirring sheet on the lower butterfly stirrer 740, and the stirring sheet on the upper butterfly stirrer 720 is inclined 45 ° to the left, and the stirring sheet on the lower butterfly stirrer 740 is inclined 45 ° to the right, so that the inclination directions of the stirring sheet on the upper butterfly stirrer 720 and the stirring sheet on the lower butterfly stirrer 740 are set opposite to each other, and the purpose that the upper butterfly stirrer 720 presses down the modified silica gel material and the lower butterfly stirrer 740 turns up the modified silica gel material can be achieved.
The rest of the present embodiment is the same as the embodiment, and the unexplained features in the present embodiment are all explained by the second embodiment, and are not described here again.
In the fourth embodiment of the present utility model, as shown in fig. 4, two double-paddle turning shafts 800 are provided; wherein the dispersion shearing shaft 700 and the anti-sticking wall scraping blade 900 are disposed on the bottom center line of the revolution main shaft 300, and the two double-paddle turning shafts 800 are symmetrically disposed at both sides of the bottom center line of the revolution main shaft 300.
Specifically, in this embodiment, two double-oar turning shafts 800 are symmetrically arranged along the bottom central line of the revolution main shaft 300, and the motions between the two double-oar turning shafts 800 are not affected by each other, so that the contact area with the modified silica gel material is increased, stirring is more sufficient, the modified silica gel material inside the kettle body 200 can be uniformly stirred in all directions under the double stirring effect, and further the modified silica gel material is uniformly stirred, so that the quality of the modified silica gel product can be effectively improved.
The rest of the present embodiment is the same as the first embodiment, and the unexplained features in the present embodiment are all explained by the first embodiment, and are not described here again.
In a fifth embodiment of the present utility model, as shown in fig. 6, the two double-paddle turning shafts 800 have the same structure, and each of the double-paddle turning shafts includes a second rotating shaft 810, a first side turning paddle 820, a second side turning paddle 830, and an upward turning pushing blade 840; the second rotating shaft 810 is rotatably installed at the bottom of the revolution main shaft 300 and is accommodated in the kettle body 200, and the second rotating shaft 810 and the rotation outer sleeve 500 are in meshed transmission; the first side turning paddle 820 and the second side turning paddle 830 are symmetrically fixed at the left and right sides of the second rotating shaft 810; the plurality of upward-turning pushing blades 840 are sequentially arranged at intervals from top to bottom along the length direction of the second rotating shaft 810 and are arranged in an arc line, and the plurality of upward-turning pushing blades 840 are all connected to the second rotating shaft 810 in a downward-inclined manner.
Specifically, in this embodiment, in the stirring production process of the modified silica gel material, on one hand, the plurality of upward turning pushing blades 840 on the double-paddle turning shaft 800 rotate along with the second rotating shaft 810 at a high speed, the modified silica gel material can be effectively lifted up through the upward turning pushing blades 840 which are inclined downward and are arranged in an arc, and on the other hand, the first side turning paddle 820 and the second side turning paddle 830 on the double-paddle turning shaft 800 rotate along with the second rotating shaft 810 at a high speed, and the lifted modified silica gel material can be effectively turned up through the first side turning paddle 820 and the second side turning paddle 830, so that the circulation of the upper and lower modified silica gel materials inside the kettle body 200 is realized.
The rest of the present embodiment is the same as the fourth embodiment, and the unexplained features in the present embodiment are all explained by the fourth embodiment, and are not described here again.
In the sixth embodiment of the present utility model, as shown in fig. 1 to 3, a first pulley 310 is provided at the top end of the revolution main shaft 300, a second pulley 410 is provided at the output shaft of the first power member 400, and the first pulley 310 and the second pulley 410 are connected by a transmission belt; the bottom end of the revolution main shaft 300 is provided with a first engagement gear 320, the top end of the dispersion shearing shaft 700 is provided with a second engagement gear 760, and the first engagement gear 320 is engaged with the second engagement gear 760.
Specifically, in the present embodiment, during the revolution of the revolution main shaft 300, the first power member 400 is firstly moved, then drives the second pulley 410 to rotate, then drives the first pulley 310 and the revolution main shaft 300 to rotate under the linkage of the transmission belt, and the dispersing shear shaft 700, the double-paddle turning shaft 800 and the anti-sticking wall scraping blade 900 revolve along with the revolution main shaft 300, and during this process, the revolution main shaft 300 drives the dispersing shear shaft 700 to synchronously rotate on the revolution main shaft 300 by utilizing the meshing transmission between the first meshing gear 320 and the second meshing gear 760.
The rest of the present embodiment is the same as the first embodiment, and the unexplained features in the present embodiment are all explained by the first embodiment, and are not described here again.
In a seventh embodiment of the present utility model, as shown in fig. 1 to 3, a first sprocket 510 is disposed at the top end of the rotating outer sleeve 500, a second sprocket 610 is disposed at the output shaft of the second power member 600, and the first sprocket 510 and the second sprocket 610 are connected by a transmission chain; the bottom end of the rotating outer sleeve 500 is provided with a third meshing gear 520, the top end of the double-paddle turning shaft 800 is provided with a fourth meshing gear 850, and the third meshing gear 520 is meshed with the fourth meshing gear 850 for transmission.
Specifically, in the present embodiment, during the rotation of the rotation outer sleeve 500, the second power member 600 is firstly actuated, then drives the second sprocket 610 to rotate, and then drives the first sprocket 510 and the rotation outer sleeve 500 to rotate under the linkage of the transmission chain, in this process, the third meshing gear 520 and the fourth meshing gear 850 are utilized to mesh and drive the rotation outer sleeve 500 to drive the double-pitch turning shaft 800 to synchronously rotate on the revolution main shaft 300.
The rest of the present embodiment is the same as the first embodiment, and the unexplained features in the present embodiment are all explained by the first embodiment, and are not described here again.
In an eighth embodiment of the present utility model, as shown in fig. 1 to 2, the process support 100 includes a setting base 110 and a process base 120; the kettle body 200 is placed in the placement base 110, and the revolution main shaft 300, the first power member 400 and the second power member 600 are mounted on the processing base 120; the processing base 120 is slidably connected to the placement base 110, that is, the processing base 120 moves along the height direction of the placement base 110, so as to drive the revolution main shaft 300, the dispersion shearing shaft 700, the double-paddle turning shaft 800 and the anti-sticking wall scraping knife 900 to approach or separate from the kettle body 200.
Specifically, in this embodiment, when a modified silica gel material needs to be added to the kettle body 200 or a modified silica gel finished product needs to be taken out from the kettle body 200, since the processing base 120 can ascend or descend relative to the placement base 110, the processing base 120 can drive the revolution main shaft 300, the dispersion shearing shaft 700, the double-paddle turning shaft 800 and the anti-sticking wall scraping knife 900 to be away from or close to the kettle body 200, so that the kettle body 200 is conveniently separated from the revolution main shaft 300, the dispersion shearing shaft 700, the double-paddle turning shaft 800 and the anti-sticking wall scraping knife 900, and the kettle body 200 can be easily taken out from the placement base 110, which is beneficial to the carrying and moving of the kettle body 200.
The rest of the present embodiment is the same as the first embodiment, and the unexplained features in the present embodiment are all explained by the first embodiment, and are not described here again.
The foregoing description of the preferred embodiments of the utility model is not intended to be limiting, but rather is intended to cover all modifications, equivalents, and alternatives falling within the spirit and principles of the utility model.
Claims (9)
1. The utility model provides a modified silica gel reation kettle of upper and lower circulation material which characterized in that includes:
machining a support;
the kettle body is arranged in the processing support, and the inside of the kettle body is hollow for storing modified silica gel materials;
the revolution main shaft part is rotatably arranged on the processing support and driven by a first power part;
the rotating outer sleeve is rotatably arranged on the revolution main shaft piece and driven by a second power piece;
the dispersing and shearing shaft is rotatably arranged at the bottom of the revolution main shaft piece and is accommodated in the kettle body, and the dispersing and shearing shaft and the revolution main shaft piece are in meshed transmission for shearing the modified silica gel material;
the double-paddle turning shaft is rotatably arranged at the bottom of the revolution main shaft piece and is accommodated in the kettle body, and the double-paddle turning shaft and the autorotation outer sleeve are in meshed transmission for turning up the modified silica gel material;
and the anti-sticking wall scraping knife is fixedly arranged at the bottom of the revolution main shaft part and is accommodated in the kettle body, wherein the anti-sticking wall scraping knife is contacted with the inner wall of the kettle body so as to scrape off the modified silica gel material on the inner wall of the kettle body.
2. The modified silica gel reaction kettle for circulating materials up and down according to claim 1, wherein: the dispersing and shearing shaft comprises a first rotating shaft, an upper butterfly stirrer, an upper dispersing disc, a lower butterfly stirrer and a lower dispersing disc; the first rotating shaft is rotatably arranged at the bottom of the revolution main shaft piece and is accommodated in the kettle body, and the first rotating shaft and the revolution main shaft piece are in meshed transmission; the upper butterfly stirrer, the upper dispersing disc, the lower butterfly stirrer and the lower dispersing disc are sequentially arranged at intervals from top to bottom along the length direction of the first rotating shaft.
3. The modified silica gel reaction kettle for circulating materials up and down according to claim 2, wherein: the inclination direction of the stirring sheets on the upper butterfly stirrer is opposite to the inclination direction of the stirring sheets on the lower butterfly stirrer; when the stirring sheet on the upper butterfly stirrer inclines leftwards, the first rotating shaft rotates clockwise; when the upper stirring blade of the upper butterfly stirrer inclines rightwards, the first rotating shaft rotates anticlockwise; so that the upper butterfly stirrer presses down the modified silica gel material, and the lower butterfly stirrer turns up the modified silica gel material.
4. A modified silica gel reaction kettle for circulating materials up and down according to claim 3, wherein: stirring sheets on the upper butterfly stirrer are inclined to the left by 45 degrees, and stirring sheets on the lower butterfly stirrer are inclined to the right by 45 degrees.
5. The modified silica gel reaction kettle for circulating materials up and down according to claim 1, wherein: the two double-paddle turning shafts are arranged; the dispersing shearing shaft and the anti-sticking wall scraping knife are arranged on the bottom middle line of the revolution main shaft, and the two double-paddle turning shafts are symmetrically arranged on two sides of the bottom middle line of the revolution main shaft.
6. The modified silica gel reaction kettle for circulating materials up and down according to claim 5, wherein: the two double-oar turning shafts have the same structure and comprise a second rotating shaft, a first side turning oar, a second side turning oar and an upward turning pushing blade; the second rotating shaft is rotatably arranged at the bottom of the revolution main shaft piece and is accommodated in the kettle body, and the second rotating shaft and the rotation outer sleeve are in meshed transmission; the first side turning paddles and the second side turning paddles are symmetrically fixed on the left side and the right side of the second rotating shaft; the upward turning pushing blades are sequentially arranged at intervals from top to bottom along the length direction of the second rotating shaft and are distributed in an arc line, and the upward turning pushing blades are connected to the second rotating shaft in a downward inclined mode.
7. The modified silica gel reaction kettle for circulating materials up and down according to claim 1, wherein: the top end of the revolution main shaft piece is provided with a first belt pulley, the output shaft of the first power piece is provided with a second belt pulley, and the first belt pulley is connected with the second belt pulley through a transmission belt; the bottom of revolution main shaft spare is provided with first meshing gear, the top of dispersion shearing axle is provided with the second meshing gear, first meshing gear with the meshing of second meshing gear is transmitted.
8. The modified silica gel reaction kettle for circulating materials up and down according to claim 1, wherein: the top end of the self-rotating outer sleeve is provided with a first sprocket, the output shaft of the second power piece is provided with a second sprocket, and the first sprocket is connected with the second sprocket through a transmission chain; the bottom of the self-rotating outer sleeve is provided with a third meshing gear, the top of the double-paddle turning shaft is provided with a fourth meshing gear, and the third meshing gear and the fourth meshing gear are in meshing transmission.
9. The modified silica gel reaction kettle for circulating materials up and down according to claim 1, wherein: the processing support comprises a placement base and a processing base; the kettle body is placed in the placement base, and the revolution main shaft piece, the first power piece and the second power piece are installed on the processing base; the processing base station is connected with the placement base station in a sliding manner, namely, the processing base station moves along the height direction of the placement base station so as to drive the revolution main shaft piece, the dispersion shearing shaft, the double-paddle turning shaft and the anti-sticking scraping wall knife to be close to or far away from the kettle body.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202322225223.5U CN220610383U (en) | 2023-08-17 | 2023-08-17 | Modified silica gel reaction kettle capable of circulating materials up and down |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202322225223.5U CN220610383U (en) | 2023-08-17 | 2023-08-17 | Modified silica gel reaction kettle capable of circulating materials up and down |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN220610383U true CN220610383U (en) | 2024-03-19 |
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ID=90218983
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202322225223.5U Active CN220610383U (en) | 2023-08-17 | 2023-08-17 | Modified silica gel reaction kettle capable of circulating materials up and down |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN220610383U (en) |
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2023
- 2023-08-17 CN CN202322225223.5U patent/CN220610383U/en active Active
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