CN219765173U - Dealcoholized silicone sealant production system - Google Patents
Dealcoholized silicone sealant production system Download PDFInfo
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- CN219765173U CN219765173U CN202320296568.7U CN202320296568U CN219765173U CN 219765173 U CN219765173 U CN 219765173U CN 202320296568 U CN202320296568 U CN 202320296568U CN 219765173 U CN219765173 U CN 219765173U
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- dealcoholization
- inlet
- silicone sealant
- production system
- mixer
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- 238000004519 manufacturing process Methods 0.000 title claims abstract description 30
- 239000004590 silicone sealant Substances 0.000 title claims abstract description 25
- 239000000853 adhesive Substances 0.000 claims abstract description 17
- 230000001070 adhesive effect Effects 0.000 claims abstract description 17
- 239000012752 auxiliary agent Substances 0.000 claims abstract description 15
- 239000000463 material Substances 0.000 claims description 28
- 238000010924 continuous production Methods 0.000 abstract description 4
- 238000000034 method Methods 0.000 abstract description 3
- 238000003756 stirring Methods 0.000 description 3
- 238000004891 communication Methods 0.000 description 2
- 239000003292 glue Substances 0.000 description 2
- 241001167839 Hymenochaete corrugata Species 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
Landscapes
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
Abstract
The utility model discloses a dealcoholized silicone sealant production system, which comprises: a dealcoholization component and a feeding component; the dealcoholization assembly comprises: the device comprises a feed inlet, a three-way valve and two dealcoholization cylinders; three ports of the three-way valve are respectively connected with the feed inlet and the two dealcoholization cylinders; the feed assembly includes: a mixer; the mixer is provided with an auxiliary agent inlet and a base adhesive inlet, and a discharge port of the mixer is communicated with the feed inlet. Through set up two dealcoholization cylinders in dealcoholization assembly for can realize two dealcoholization cylinders and use in turn through the break-make between three-way valve control feed inlet and the two dealcoholization cylinders, thereby need not to pass through the process of changing dealcoholization cylinder, can improve work efficiency, solve the unable continuous production of current silicone sealant and lead to the lower problem of production efficiency.
Description
Technical Field
The utility model relates to the technical field of silicone sealant production, in particular to a dealcoholized silicone sealant production system.
Background
In the production process of the traditional silicone sealant, a certain proportion of base glue and auxiliary agent are generally added into a material cylinder, the material cylinder is moved to a station of a stirrer for stirring and vacuumizing, stirring is stopped after the stirring is completed, and the material cylinder is moved to a station of a hydraulic discharging machine for sub-packaging. Because the material cylinder needs to be transferred between different stations, the production process cannot be continuous, and the production efficiency is affected.
Disclosure of Invention
Therefore, the utility model aims to provide a dealcoholized silicone sealant production system which is used for solving the problem that the production efficiency is low due to the fact that the existing silicone sealant cannot be continuously produced.
In order to achieve the above technical object, the present utility model provides a dealcoholized silicone sealant production system, comprising: a dealcoholization component and a feeding component;
the dealcoholization assembly comprises: the device comprises a feed inlet, a three-way valve and two dealcoholization cylinders;
three ports of the three-way valve are respectively connected with the feed inlet and the two dealcoholization cylinders;
the feed assembly includes: a mixer;
the mixer is provided with an auxiliary agent inlet and a base adhesive inlet, and a discharge port of the mixer is communicated with the feed inlet.
Further, the auxiliary agent inlet and/or the base adhesive inlet are/is provided with a quantitative feeder.
Further, the mixer is also provided with a color paste inlet.
Further, the color paste inlet is provided with a quantitative feeder.
Further, a premixing core and a mixing core are sequentially arranged in the mixer along a path through which materials pass.
Further, a booster cylinder is arranged between the premixing core and the mixing core.
Further, the mixer is also provided with a circulating pump and a circulating pipe;
two ends of the circulating pipe are respectively communicated with the premixing core and the mixing core;
the circulating pump is connected with the circulating pipe.
Further, a presser is also arranged between the base adhesive inlet and the premixing core.
Further, the dealcoholization assembly further comprises: a three-way pipe;
the three-way pipe is respectively connected with the discharge ports of the two dealcoholization cylinders.
Further, the dealcoholization component is also provided with a vacuum tube;
the vacuum tube is communicated with the two dealcoholization cylinders.
According to the technical scheme, the utility model provides a dealcoholized silicone sealant production system, which comprises: a dealcoholization component and a feeding component; the dealcoholization assembly comprises: the device comprises a feed inlet, a three-way valve and two dealcoholization cylinders; three ports of the three-way valve are respectively connected with the feed inlet and the two dealcoholization cylinders; the feed assembly includes: a mixer; the mixer is provided with an auxiliary agent inlet and a base adhesive inlet, and a discharge port of the mixer is communicated with the feed inlet. Through set up two dealcoholization cylinders in dealcoholization assembly for can realize two dealcoholization cylinders and use in turn through the break-make between three-way valve control feed inlet and the two dealcoholization cylinders, thereby need not to pass through the process of changing dealcoholization cylinder, can improve work efficiency, solve the unable continuous production of current silicone sealant and lead to the lower problem of production efficiency.
Drawings
In order to more clearly illustrate the embodiments of the utility model or the technical solutions of the prior art, the drawings which are used in the description of the embodiments or the prior art will be briefly described, it being obvious that the drawings in the description below are only some embodiments of the utility model, and that other drawings can be obtained from these drawings without inventive faculty for a person skilled in the art.
Fig. 1 is a schematic diagram of the overall structure of a dealcoholized silicone sealant production system according to an embodiment of the present utility model.
Detailed Description
The following description of the embodiments of the present utility model will be made clearly and fully with reference to the accompanying drawings, in which it is evident that the embodiments described are some, but not all embodiments of the utility model. All other embodiments, which can be made by one of ordinary skill in the art without undue burden from the utility model, are intended to be within the scope of the claimed utility model based on embodiments of the present utility model.
In the description of the embodiments of the present utility model, it should be noted that the terms "center," "upper," "lower," "left," "right," "vertical," "horizontal," "inner," "outer," and the like indicate or are based on the orientation or positional relationship shown in the drawings, merely to facilitate description of the embodiments of the present utility model and to simplify the 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 embodiments of the present utility model. Furthermore, the terms "first," "second," and "third" are used for descriptive purposes only and are not to be construed as indicating or implying relative importance.
In describing embodiments of the present utility model, it should be noted that, unless explicitly stated and limited otherwise, the terms "mounted," "connected," and "connected" are to be construed broadly, and may be, for example, fixedly connected, interchangeably connected, integrally connected, mechanically connected, electrically connected, directly connected, indirectly connected through an intermediary, or in communication between two elements. The specific meaning of the above terms in embodiments of the present utility model will be understood in detail by those of ordinary skill in the art.
Referring to fig. 1, a dealcoholized silicone sealant production system provided in an embodiment of the utility model includes: a dealcoholization assembly 10 and a feed assembly 20; the dealcoholization assembly 10 includes: a feed inlet 11, a three-way valve 12 and two dealcoholization cylinders 13; three ports of the three-way valve 12 are respectively connected with the feed inlet 11 and the two dealcoholization cylinders 13; the feed assembly 20 includes: a mixer 21; the mixer 21 is provided with an auxiliary agent inlet 22 and a base adhesive inlet 23, and a discharge port of the mixer 21 is communicated with the feed port 11.
Wherein a mixing pipe for mixing materials is arranged in the mixer 21. The mixing tube is communicated with the auxiliary agent inlet 22 and the base adhesive inlet 23, so that the auxiliary agent and the base adhesive can enter the mixing tube through the auxiliary agent inlet 22 and the base adhesive inlet 23 respectively for mixing. The mixed materials can enter the feed inlet 11 through the discharge port of the mixer 21, and then enter a dealcoholization cylinder 13 through the three-way valve 12 for dealcoholization; when the materials are discharged after the dealcoholization of one dealcoholization cylinder 13 is completed, the materials in the mixer 21 can enter the other dealcoholization cylinder 13 through the three-way valve 12 to carry out dealcoholization procedures, so that the two dealcoholization cylinders 13 are alternately used for continuous production, the production efficiency is improved, and the phenomenon of material overflow caused by material transfer is avoided.
In one embodiment, the auxiliary agent inlet 22 and/or the base adhesive inlet 23 are provided with a dosing device 24. For example, both the auxiliary agent inlet 22 and the base adhesive inlet 23 may be provided with a dosing device 24, the dosing device 24 being controlled by a servo motor. By metering by the quantitative feeder 24, the feeding speed and feeding amount of the auxiliary agent and the base adhesive can be adjusted so that the auxiliary agent and the base adhesive are synchronously fed. Meanwhile, the current real-time feeding speed can be judged through a servo motor connected with the quantitative feeder 24.
Further, the mixer 21 is also provided with a color paste inlet 25.
Similarly, the color paste inlet 25 is in communication with the mixing tube for mixing the color paste with the material.
Further, the color paste inlet 25 is provided with a quantitative feeder 24 so that the feeding amount and feeding speed of the color paste can be controlled by the quantitative feeder 24.
Further, a premixing core 211 and a mixing core 212 are sequentially disposed along a path through which the materials pass in the mixer 21.
Specifically, premix core 211 is a low drag mix core; both the premixing core 211 and the mixing core 212 are arranged in the mixing pipe, and materials can enter the mixing pipe to mix the materials. The resistance becomes high instantaneously because of the high viscosity peak generated when the materials are mixed. Therefore, in this embodiment, in order to ensure that the materials smoothly pass through the viscosity peak and achieve the mixing purpose, the premixing core 211 is provided in this scheme, so that the materials can be premixed with low resistance and then transferred to the mixing core 212 for mixing, and the materials are ensured not to be affected by the viscosity peak when being mixed by the mixing core 212, so that the uniformity of material mixing can be improved.
Further, a pressurizing cylinder 213 is provided between the premix core 211 and the mix core 212.
By pressurizing cylinder 213, the pressure inside mixing core 212 can be increased, and the degree of mixing of the materials can be improved.
In another embodiment, the mixer 21 is further provided with a circulation pump 214 and a circulation pipe 215; two ends of the circulation pipe 215 are respectively communicated with the premixing core 211 and the mixing core 212; the circulation pump 214 is connected to the circulation pipe 215.
Specifically, both ends of the circulation pipe 215 are connected to the premix core 211 and the mix core 212 through openable and closable valves. After mixing the mixing core 212, the mixed materials can enter the circulating pipe 215 and return to the premixing core 211 under the condition that the valve and the circulating pump 214 are opened, so that the materials are mixed again, and the situation that the materials are mixed unevenly to cause dry glue crust in the pipeline is avoided.
Further, a presser 26 is provided between the base adhesive inlet 23 and the premix core 211.
The presser 26 may be a ram presser that pushes material from the base glue inlet 23 into the premix core 211.
Further, the dealcoholization assembly 10 further comprises: tee 14; the tee pipe 14 is respectively connected with the discharge ports of the two dealcoholization cylinders 13. Namely, the discharge ports of the two dealcoholization cylinders 13 are collected through the tee pipe 14, so that dealcoholized materials can be conveniently collected.
Further, the dealcoholization assembly 10 is also provided with a vacuum tube 15; the vacuum tube 15 communicates with the two dealcoholization cylinders 13.
Specifically, vacuum tube 15 is used to draw a vacuum on dealcoholization cylinder 13.
The dealcoholized silicone sealant production system provided by the scheme can realize continuous production, and supplies materials to enter the mixer 21 for mixing at a fixed speed quantitatively, so that staff can control each production link conveniently, and the production efficiency can be improved.
While the utility model has been described in detail with reference to the examples, it will be apparent to those skilled in the art that the foregoing description of the preferred embodiments of the utility model may be modified or equivalents may be substituted for elements thereof, and that any modifications, equivalents, improvements or changes will fall within the spirit and principles of the utility model.
Claims (10)
1. A dealcoholized silicone sealant production system, comprising: a dealcoholization assembly (10) and a feed assembly (20);
the dealcoholization assembly (10) includes: a feed inlet (11), a three-way valve (12) and two dealcoholization cylinders (13);
three ports of the three-way valve (12) are respectively connected with the feed inlet (11) and the two dealcoholization cylinders (13);
the feed assembly (20) comprises: a mixer (21);
the mixer (21) is provided with an auxiliary agent inlet (22) and a base adhesive inlet (23), and a discharge port of the mixer (21) is communicated with the feed inlet (11).
2. The dealcoholized silicone sealant production system according to claim 1, wherein the auxiliary agent inlet (22) and/or the base adhesive inlet (23) is provided with a quantitative feeder (24).
3. The dealcoholized silicone sealant production system according to claim 1 or 2, wherein the mixer (21) is further provided with a color paste inlet (25).
4. A dealcoholized silicone sealant production system according to claim 3, wherein the color paste inlet (25) is provided with a quantitative feeder (24).
5. The dealcoholized silicone sealant production system according to claim 1, wherein a premixing core (211) and a mixing core (212) are sequentially arranged in the mixer (21) along a path through which materials pass.
6. The dealcoholized silicone sealant production system according to claim 5, wherein a pressurizing cylinder (213) is provided between the pre-mixing core (211) and the mixing core (212).
7. The dealcoholized silicone sealant production system according to claim 5 or 6, wherein the mixer (21) is further provided with a circulation pump (214) and a circulation pipe (215);
two ends of the circulating pipe (215) are respectively communicated with the premixing core (211) and the mixing core (212);
the circulating pump (214) is connected with the circulating pipe (215).
8. The dealcoholized silicone sealant production system according to claim 5 or 6, wherein a presser (26) is further provided between the base adhesive inlet (23) and the premix core (211).
9. The dealcoholized silicone sealant production system according to claim 1, wherein the dealcoholization assembly (10) further comprises: a tee (14);
the tee pipe (14) is respectively connected with the discharge ports of the two dealcoholization cylinders (13).
10. The dealcoholized silicone sealant production system according to claim 1, wherein said dealcoholization assembly (10) is further provided with a vacuum tube (15);
the vacuum tube (15) is communicated with the two dealcoholization cylinders (13).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202320296568.7U CN219765173U (en) | 2023-02-23 | 2023-02-23 | Dealcoholized silicone sealant production system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202320296568.7U CN219765173U (en) | 2023-02-23 | 2023-02-23 | Dealcoholized silicone sealant production system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN219765173U true CN219765173U (en) | 2023-09-29 |
Family
ID=88129101
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202320296568.7U Active CN219765173U (en) | 2023-02-23 | 2023-02-23 | Dealcoholized silicone sealant production system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN219765173U (en) |
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2023
- 2023-02-23 CN CN202320296568.7U patent/CN219765173U/en active Active
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