CN220803214U - Organic silicon monomer hydrolysis tank - Google Patents

Organic silicon monomer hydrolysis tank Download PDF

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Publication number
CN220803214U
CN220803214U CN202322285596.1U CN202322285596U CN220803214U CN 220803214 U CN220803214 U CN 220803214U CN 202322285596 U CN202322285596 U CN 202322285596U CN 220803214 U CN220803214 U CN 220803214U
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linkage
seat
hydrolysis tank
supporting
fixed
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CN202322285596.1U
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Chinese (zh)
Inventor
陈建宇
陈一诺
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Dongzhi Oasis Environmental Protection Chemical Co Ltd
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Dongzhi Oasis Environmental Protection Chemical Co Ltd
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Abstract

The utility model provides an organosilicon monomer hydrolysis tank which comprises a hydrolysis tank body, a supporting seat, a linkage seat and stirring paddles, wherein the supporting seat is connected with a supporting mechanism, the supporting seat is connected above the hydrolysis tank body through the supporting mechanism, the linkage seat is rotatably connected at the center of the supporting seat through a bearing, and part of the linkage seat is positioned in the hydrolysis tank body. According to the utility model, the servo motor in the linkage mechanism drives the driving fluted disc to rotate so as to enable the driven fluted disc to be meshed and linked, the linkage seat and the stirring blade are driven to integrally rotate so as to achieve the stirring effect on the hydrolysis tank, and the rack is driven to move up and down through the up-and-down movement of the telescopic part of the air cylinder while rotating, and the linkage gear is driven to be meshed and linked so as to drive the stirring blade to rotate so as to change the angle of the stirring blade, and the stirring blade can change the stirring effect on the water body while horizontally rotating so as to effectively avoid vortex generation during stirring.

Description

Organic silicon monomer hydrolysis tank
Technical Field
The utility model relates to the technical field of hydrolysis tanks, in particular to an organosilicon monomer hydrolysis tank.
Background
The organic silicon is an organic material used in various industries in life, the organic silicon in actual use is formed by Dn rings, and the organic silicon which needs to be obtained in practical is obtained by hydrolyzing organic silicon monomers, so that the organic silicon monomers are often required to be placed in a hydrolysis tank for hydrolysis during production, however, in the conventional hydrolysis tank for hydrolyzing the organic silicon, in order to improve the hydrolysis efficiency, a stirring mechanism is generally arranged in the hydrolysis tank for stirring the organic silicon, but most stirring mechanisms at present rotate through a motor driving stirring blade, so that the stirring effect on a water body is realized, the angle of the blade is mostly fixed, the blade with the fixed angle can generate vortex in the hydrolysis tank during rotation, the hydrolysis efficiency is not improved, the water level at the edge of the hydrolysis tank is raised, the water body overflows from the hydrolysis tank, if a motor is made to alternately rotate, a certain time is consumed during the positive and negative alternation, and the hydrolysis efficiency is influenced.
Disclosure of utility model
Aiming at the defects of the prior art, the utility model provides an organosilicon monomer hydrolysis tank.
The utility model solves the technical problems by the following technical means:
The utility model provides an organosilicon monomer pond of hydrolysising, including the pond of hydrolysising, the supporting seat, linkage seat and stirring paddle, be connected with supporting mechanism on the supporting seat, and the supporting seat passes through supporting mechanism and connects in the pond top of hydrolysising, the linkage seat passes through the center department of bearing rotation connection at the supporting seat, and its part is located the pond of hydrolysising inside, be provided with link gear on the linkage seat, link gear includes supporting plate and linkage subassembly, the supporting plate passes through the round bar level to be fixed in the top of supporting seat, and the top of linkage seat passes through bearing and supporting plate rotation to be connected, stirring paddle passes through angle adjustment mechanism to be connected on the linkage seat, it is located the pond of hydrolysising inside, angle adjustment mechanism includes the docking pole, the linkage gear, cylinder and rack, and stirring paddle are fixed in the one end of docking pole, and docking pole rotation is connected on the linkage seat, the linkage gear is fixed at the other end of docking pole, it is located the internal cavity of linkage seat, rack and linkage gear meshing, and its sliding connection is in the inside of linkage seat, and the telescopic part of connection at the cylinder, the fixed part of cylinder is connected on the supporting.
Preferably, the stirring paddles and the racks are symmetrically provided with two groups, and the two groups of racks are oppositely arranged and are meshed with the linkage gear.
Preferably, the linkage assembly comprises a driven fluted disc, a servo motor and a driving fluted disc, wherein the driven fluted disc is fixed at the top end of the outer wall of the linkage seat, the servo motor is fixed on the bearing plate, and the driving fluted disc is connected to the output shaft of the servo motor and meshed with the driven fluted disc.
Preferably, the driven toothed disc has a diameter twice that of the driving toothed disc.
Preferably, the supporting mechanism comprises a supporting rod and a sliding block, the supporting rod is of an L-shaped structure, one end of the supporting rod is slidably connected in the supporting seat, the supporting rod is locked through a screw, the sliding block is fixed at the other end of the supporting rod, and the sliding block is slidably connected on the hydrolysis tank.
Preferably, guide rails are fixed on two sides of the top of the hydrolysis tank, the cross sections of the guide rails are of an I-shaped structure, notches of the I-shaped structure are formed in the sliding blocks in a penetrating mode, and the sliding blocks are clamped with the guide rails in a matching mode through the notches.
The utility model has the beneficial effects that: the servo motor in the linkage mechanism drives the driving fluted disc to rotate so as to enable the driven fluted disc to be meshed and linked, the linkage seat and the stirring paddle are driven to integrally rotate so as to achieve the stirring effect on the hydrolysis tank, and the up-and-down motion of the cylinder telescopic part drives the rack to move up and down when rotating, and the rack moves up and down when rotating due to the fact that the cylinder telescopic part is connected with the rack in a rotating mode, and drives the linkage gear to be meshed and linked, so that the stirring paddle is driven to rotate so as to enable the angle of the stirring paddle to change, and the stirring effect on a water body can be changed when the stirring paddle rotates horizontally, so that vortex generation during stirring is effectively avoided.
Drawings
FIG. 1 is a schematic perspective view of an organosilicon monomer hydrolysis tank according to an embodiment of the utility model;
FIG. 2 is a schematic structural view of a support mechanism of an organosilicon monomer hydrolysis tank according to an embodiment of the utility model;
FIG. 3 is a schematic structural view of a linkage mechanism of an organosilicon monomer hydrolysis tank according to an embodiment of the utility model;
FIG. 4 is a schematic view of an angle adjusting mechanism of an organosilicon monomer hydrolysis tank according to an embodiment of the utility model;
In the figure: 1. a hydrolysis tank; 2. a support base; 21. a brace rod; 22. a slide block; 23. a guide rail; 3. a linkage seat; 31. a bearing plate; 32. a driven fluted disc; 33. a servo motor; 34. a driving fluted disc; 4. stirring paddles; 41. a butt joint rod; 42. a linkage gear; 43. a cylinder; 44. a rack.
Detailed Description
In order to make the objects, technical solutions and advantages of the embodiments of the present utility model more apparent, the technical solutions of the present utility model will be clearly and completely described below with reference to the embodiments.
Examples
As shown in fig. 1-4, in this embodiment, the organic silicon monomer hydrolysis tank comprises a hydrolysis tank 1, a support seat 2, a linkage seat 3 and a stirring blade 4, wherein the support seat 2 is connected with a support mechanism, the support seat 2 is connected above the hydrolysis tank 1 through the support mechanism, the linkage seat 3 is rotatably connected at the center of the support seat 2 through a bearing, and part of the linkage seat is positioned in the hydrolysis tank 1, the linkage seat 3 is provided with a linkage mechanism, the linkage mechanism comprises a bearing plate 31 and a linkage assembly, the bearing plate 31 is horizontally fixed above the support seat 2 through a round bar, the top end of the linkage seat 3 is rotatably connected with the bearing plate 31 through a bearing, the stirring blade 4 is connected on the linkage seat 3 through an angle adjusting mechanism, the angle adjusting mechanism comprises a docking bar 41, a linkage gear 42, a cylinder 43 and a rack 44, the stirring blade 4 is fixed at one end of the docking bar 41, the butt-joint rod 41 is rotationally connected to the linkage seat 3, the linkage gear 42 is fixed at the other end of the butt-joint rod 41 and is positioned in the inner cavity of the linkage seat 3, the rack 44 is meshed with the linkage gear 42 and is slidingly connected to the inside of the linkage seat 3, and is rotationally connected to the telescopic part of the air cylinder 43, the fixed part of the air cylinder 43 is connected to the bearing plate 31, specifically, when in use, the servo motor 33 in the linkage mechanism drives the driving fluted disc 34 to rotate so as to drive the driven fluted disc 32 to be meshed and linked, the linkage seat 3 and the stirring blade 4 are driven to integrally rotate so as to realize the stirring effect on the hydrolysis tank 1, and when in rotation, the telescopic part of the air cylinder 43 is rotationally connected with the rack 44, the rack 44 is rotationally moved up and down and drives the linkage gear 42 to be meshed and linked, and then drive stirring paddle 4 rotation and make its angle change, through the regulation to stirring paddle 4's angle, and then make stirring paddle 4 can change the stirring effect to the water in the horizontal rotation, and then effectually avoided the production of vortex when stirring.
As shown in fig. 1-4, in some embodiments, two sets of stirring paddles 4 and racks 44 are symmetrically disposed, and the two sets of racks 44 are disposed opposite each other and are engaged with the linkage gear 42, so that the two stirring paddles 4 can rotate synchronously and reversely through the oppositely disposed racks 44.
As shown in fig. 1-3, in some embodiments, the linkage assembly includes a driven fluted disc 32, a servo motor 33 and a driving fluted disc 34, the driven fluted disc 32 is fixed on the top end of the outer wall of the linkage seat 3, the servo motor 33 is fixed on the bearing plate 31, the driving fluted disc 34 is connected on the output shaft of the servo motor 33 and is meshed with the driven fluted disc 32, the driving fluted disc 34 is driven to rotate by the servo motor 33, and then the driven fluted disc 32 is driven to mesh and link, so that the linkage seat 3 can rotate synchronously as a whole.
As shown in fig. 1-3, in some embodiments, the driven cog 32 has a diameter twice that of the driving cog 34, reducing the load on the servo motor 33.
As shown in fig. 1-2, in some embodiments, the supporting mechanism includes a supporting rod 21 and a sliding block 22, the supporting rod 21 is in an L-shaped structure, one end of the supporting rod 21 is slidably connected inside the supporting seat 2 and locked by a screw, the sliding block 22 is fixed at the other end of the supporting rod 21, and the sliding block 22 is slidably connected on the hydrolysis tank 1, the supporting seat 2 is integrally supported by the supporting rod 21 so as to be located above the hydrolysis tank 1, and a worker can adjust the interval between two adjacent supporting rods 21 according to the actual size of the hydrolysis tank 1.
As shown in fig. 1-2, in some embodiments, two sides of the top of the hydrolysis tank 1 are fixed with guide rails 23, the section of the guide rails 23 is in an i-shaped structure, and notches with the i-shaped structure are formed in the sliding blocks 22 in a penetrating manner, and the sliding blocks 22 are clamped with the guide rails 23 in a matching manner through the notches, so that a worker can adjust the positions of the supporting seat 2 and the whole structure thereof on the hydrolysis tank 1 as required.
The above embodiments are only for illustrating the technical solution of the present utility model, and are not limiting.

Claims (6)

1. The organic silicon monomer hydrolysis tank comprises a hydrolysis tank (1), a supporting seat (2), a linkage seat (3) and stirring paddles (4), and is characterized in that: the support seat (2) is connected with a support mechanism, the support seat (2) is connected above the hydrolysis tank (1) through the support mechanism, the linkage seat (3) is rotationally connected to the center of the support seat (2) through a bearing, part of the linkage seat is positioned inside the hydrolysis tank (1), the linkage seat (3) is provided with the linkage mechanism, the linkage mechanism comprises a bearing plate (31) and a linkage assembly, the bearing plate (31) is horizontally fixed above the support seat (2) through a round rod, the top end of the linkage seat (3) is rotationally connected with the bearing plate (31) through a bearing, the stirring blade (4) is connected to the linkage seat (3) through an angle adjusting mechanism, the stirring blade is positioned inside the hydrolysis tank (1), the angle adjusting mechanism comprises a butt joint rod (41), a linkage gear (42), an air cylinder (43) and a rack (44), the stirring blade (4) is fixed at one end of the butt joint rod (41) and rotationally connected to the seat (3), the linkage gear (42) is fixed at one end of the butt joint rod (41), the other end of the butt joint rod (41) is rotationally connected to the air cylinder (3) and is in the linkage seat (3) and is in sliding connection with the air cylinder (43) in the linkage seat (3) through the linkage mechanism, the other end of the butt rod is in the linkage gear (41) and is in the sliding connection with the air cylinder (43), the fixed part of the air cylinder (43) is connected to the bearing plate (31).
2. The silicone monomer hydrolysis cell of claim 1, wherein: the stirring paddles (4) and the racks (44) are symmetrically provided with two groups, and the two groups of racks (44) are oppositely arranged and are meshed with the linkage gear (42).
3. The silicone monomer hydrolysis cell of claim 1, wherein: the linkage assembly comprises a driven fluted disc (32), a servo motor (33) and a driving fluted disc (34), wherein the driven fluted disc (32) is fixed at the top end of the outer wall of the linkage seat (3), the servo motor (33) is fixed on the supporting plate (31), and the driving fluted disc (34) is connected to the output shaft of the servo motor (33) and meshed with the driven fluted disc (32).
4. A silicone monomer hydrolysis cell according to claim 3, characterized in that: the driven toothed disc (32) has a diameter twice that of the driving toothed disc (34).
5. The silicone monomer hydrolysis cell of claim 1, wherein: the supporting mechanism comprises a supporting rod (21) and a sliding block (22), wherein the supporting rod (21) is of an L-shaped structure, one end of the supporting rod is slidably connected to the inside of the supporting seat (2) and locked through screws, the sliding block (22) is fixed to the other end of the supporting rod (21), and the sliding block (22) is slidably connected to the hydrolysis tank (1).
6. The silicone monomer hydrolysis cell of claim 5, wherein: guide rails (23) are fixed on two sides of the top of the hydrolysis tank (1), the section of each guide rail (23) is of an I-shaped structure, a notch of the I-shaped structure is formed in the sliding block (22) in a penetrating mode, and the sliding block (22) is clamped with the guide rails (23) through the notches in a matching mode.
CN202322285596.1U 2023-08-24 2023-08-24 Organic silicon monomer hydrolysis tank Active CN220803214U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202322285596.1U CN220803214U (en) 2023-08-24 2023-08-24 Organic silicon monomer hydrolysis tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202322285596.1U CN220803214U (en) 2023-08-24 2023-08-24 Organic silicon monomer hydrolysis tank

Publications (1)

Publication Number Publication Date
CN220803214U true CN220803214U (en) 2024-04-19

Family

ID=90705746

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202322285596.1U Active CN220803214U (en) 2023-08-24 2023-08-24 Organic silicon monomer hydrolysis tank

Country Status (1)

Country Link
CN (1) CN220803214U (en)

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