CN214131610U - Continuous hydrolysis and condensation device for organic silicon resin - Google Patents
Continuous hydrolysis and condensation device for organic silicon resin Download PDFInfo
- Publication number
- CN214131610U CN214131610U CN202120001892.2U CN202120001892U CN214131610U CN 214131610 U CN214131610 U CN 214131610U CN 202120001892 U CN202120001892 U CN 202120001892U CN 214131610 U CN214131610 U CN 214131610U
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- China
- Prior art keywords
- pipe
- circulating pipe
- decomposition
- condensation device
- decomposition tank
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- Expired - Fee Related
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- 229920005989 resin Polymers 0.000 title claims abstract description 43
- 239000011347 resin Substances 0.000 title claims abstract description 43
- 238000009833 condensation Methods 0.000 title claims abstract description 37
- 230000005494 condensation Effects 0.000 title claims abstract description 37
- 230000007062 hydrolysis Effects 0.000 title claims abstract description 30
- 238000006460 hydrolysis reaction Methods 0.000 title claims abstract description 30
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 title claims description 39
- 229910052710 silicon Inorganic materials 0.000 title claims description 37
- 239000010703 silicon Substances 0.000 title claims description 37
- 238000000354 decomposition reaction Methods 0.000 claims abstract description 62
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 29
- 229920002050 silicone resin Polymers 0.000 claims abstract description 26
- 238000006243 chemical reaction Methods 0.000 claims abstract description 21
- 238000005485 electric heating Methods 0.000 claims abstract description 19
- 238000003756 stirring Methods 0.000 claims description 13
- 238000002156 mixing Methods 0.000 claims description 6
- 230000005540 biological transmission Effects 0.000 claims description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 125000000962 organic group Chemical group 0.000 description 2
- 238000003466 welding Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 125000004430 oxygen atom Chemical group O* 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 229920001296 polysiloxane Polymers 0.000 description 1
- -1 polysiloxane Polymers 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
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- Silicon Polymers (AREA)
Abstract
The utility model discloses a continuous condensation device that hydrolysises of organosilicon resin, including decomposition tank, electric heating pipe and operation panel, decomposition tank top is provided with the water pitcher, water pitcher below one side is provided with circulating pipe one, circulating pipe one side is provided with circulating pipe two, circulating pipe one with circulating pipe two tops all are provided with the suction pump, the decomposition tank inboard is provided with electric heating pipe, electric heating pipe one side is provided with the operation panel, the water pitcher with the decomposition tank is pegged graft, circulating pipe one with the decomposition tank is pegged graft. Has the advantages that: the utility model discloses a set up circulating pipe one, circulating pipe two, decomposition tank and electric heating pipe, not only can carry out continuous water decomposition to silicone resin, avoid silicone resin decomposition speed to cause water decomposition to run off slowly, but also can heat organosilicon, avoid silicone resin decomposition temperature to hang down and cause reaction efficiency low, improved the efficiency of silicone resin continuous hydrolysis condensation device work.
Description
Technical Field
The utility model relates to a condensation device technical field, concretely relates to organic silicon resin continuous hydrolysis condensation device.
Background
The organic silicon resin (also called polysiloxane) is a general name of a polymer which is formed by alternately connecting silicon atoms and oxygen atoms to form a framework, and different organic groups are connected with the silicon atoms, wherein the organic silicon resin structure contains both organic groups and inorganic structures, and the special composition and molecular structure enable the organic silicon resin to integrate the characteristics of organic matters and the functions of inorganic matters.
At present, most of the existing continuous hydrolysis and condensation devices for organic silicon resin adopt direct decomposition, water decomposition loss is easily caused by slow decomposition speed of the organic silicon resin due to lack of a circulating part, reaction efficiency is low due to low decomposition temperature of the organic silicon resin due to lack of a heating part, and working efficiency of the continuous hydrolysis and condensation device for organic silicon resin is reduced.
SUMMERY OF THE UTILITY MODEL
Technical problem to be solved
In order to overcome the defects of the prior art, the organic silicon resin continuous hydrolysis and condensation device is provided, and the problems that the organic silicon resin is easy to decompose at a low speed to cause water decomposition loss due to the lack of a circulating part, the organic silicon resin is easy to decompose at a low temperature to cause low reaction efficiency due to the lack of a heating part, and the working efficiency of the organic silicon resin continuous hydrolysis and condensation device is reduced in the prior art are solved.
(II) technical scheme
The utility model discloses a following technical scheme realizes: the utility model provides a condensation device is hydrolysised in succession to organic silicon resin, including decomposition tank, electric heating pipe and operation panel, decomposition tank top is provided with the water pitcher, water pitcher below one side is provided with circulating pipe one, circulating pipe one side is provided with circulating pipe two, circulating pipe one with circulating pipe two tops all are provided with the suction pump, decomposition tank inboard is provided with electric heating pipe, electric heating pipe one side is provided with the operation panel, the water pitcher with decomposition tank pegs graft, circulating pipe one with decomposition tank pegs graft, circulating pipe two with decomposition tank pegs graft, the suction pump with circulating pipe one and circulating pipe two all pass through screw connection, electric heating pipe with decomposition tank passes through screw connection, decomposition tank with the operation panel passes through the draw-in groove and connects.
Further, a frame column is arranged below the operating platform, and a discharge pipe is arranged between the frame columns.
By adopting the technical scheme, the frame column can enable the operating platform to be stably supported.
Further, the delivery pipe below is connected with the conveyer pipe, the conveyer pipe middle part is provided with the solenoid valve, solenoid valve one side is provided with reation kettle, there is the motor reation kettle top through screwed connection, the motor drive output is connected with the (mixing) shaft, the (mixing) shaft below is provided with the support column, the support column top is provided with operating panel.
Through adopting above-mentioned technical scheme, through the support column can make reation kettle steadily supports.
Further, the frame column is welded with the operating platform, the discharge pipe is welded with the decomposition tank, and the first circulating pipe and the second circulating pipe are both inserted into the discharge pipe.
Through adopting above-mentioned technical scheme, can discharge the resin after the decomposition through the delivery pipe.
Further, the delivery pipe is inserted into the discharge pipe, and the electromagnetic valve is connected with the delivery pipe through threads.
By adopting the technical scheme, the decomposed resin in the conveying pipe can be conveyed through the electromagnetic valve.
Further, the conveying pipe is inserted into the reaction kettle, and the stirring shaft is connected with the motor through a key.
By adopting the technical scheme, the stirring shaft can stir the decomposed resin by rotating the motor, so that the resin is condensed after decomposition.
Further, the support column is welded with the reaction kettle, and the operation panel is connected with the reaction kettle through screws.
By adopting the technical scheme, the device can be controlled through the operation panel.
(III) advantageous effects
Compared with the prior art, the utility model, following beneficial effect has:
1. the utility model discloses a set up circulating pipe one, circulating pipe two, decomposing tank and electric heating pipe, not only can carry out continuous water decomposition to silicone resin, avoid silicone resin decomposition speed to cause water to decompose and run off slowly, but also can heat organosilicon, avoid silicone resin decomposition temperature to cause reaction inefficiency, improved silicone resin continuous hydrolysis condensation device work efficiency;
2. for solving current organic silicon resin continuous hydrolysis condensation device and mostly carrying out static condensation after water decomposes, owing to lack the stirring part, the organic silicon resin condensation efficiency after making the decomposition easily causes reaction quality poor slowly, can not satisfy the problem of organic silicon resin continuous hydrolysis condensation device user demand, the utility model discloses a set up reation kettle, motor and (mixing) shaft, can stir the organic silicon resin after the decomposition, the organic silicon resin condensation efficiency after avoiding decomposing causes reaction quality poor slowly, satisfies the demand that organic silicon resin continuous hydrolysis condensation device used.
Drawings
FIG. 1 is a schematic structural view of a continuous hydrolysis and condensation device for silicone resin according to the present invention;
FIG. 2 is a front sectional view of a continuous hydrolysis and condensation apparatus for silicone resin according to the present invention;
FIG. 3 is a block circuit diagram of a continuous hydrolysis and condensation device for silicone resin.
The reference numerals are explained below:
1. a decomposition tank; 2. a water tank; 3. a first circulating pipe; 4. a second circulating pipe; 5. a water pump; 6. an electric heating tube; 7. an operation table; 8. a frame column; 9. a discharge pipe; 10. a delivery pipe; 11. an electromagnetic valve; 12. a reaction kettle; 13. a motor; 14. a stirring shaft; 15. a support pillar; 16. an operation panel.
Detailed Description
In order to make the objects, technical solutions and advantages of the present invention more clearly understood, the present invention is further described in detail below with reference to the accompanying drawings and embodiments. It should be understood that the specific embodiments described herein are merely illustrative of the invention and are not intended to limit the invention.
As shown in fig. 1-3, the continuous hydrolysis and condensation device for silicone resin in this embodiment includes a decomposition tank 1, an electric heating tube 6 and an operation table 7, a water tank 2 is disposed above the decomposition tank 1, a first circulation tube 3 is disposed on one side below the water tank 2, a second circulation tube 4 is disposed on one side of the first circulation tube 3, water pumps 5 are disposed above the first circulation tube 3 and the second circulation tube 4, the electric heating tube 6 is disposed inside the decomposition tank 1, the operation table 7 is disposed on one side of the electric heating tube 6, frame columns 8 are disposed below the operation table 7, a discharge tube 9 is disposed between the frame columns 8, the operation table 7 can be stably supported by the frame columns 8, a delivery tube 10 is connected below the discharge tube 9, an electromagnetic valve 11 is disposed in the middle of the delivery tube 10, a reaction kettle 12 is disposed on one side of the electromagnetic valve 11, a motor 13 is connected above the reaction kettle 12 by screws, a stirring shaft 14 is connected to a transmission output end of the motor 13, stirring shaft 14 below is provided with support column 15, support column 15 top is provided with operating panel 16, can make reation kettle 12 steadily support through support column 15, frame post 8 and operation panel 7 welding, delivery pipe 9 and decomposition jar 1 welding, circulating pipe one 3 and circulating pipe two 4 all peg graft with delivery pipe 9, can discharge the resin after the decomposition through delivery pipe 9, delivery pipe 10 pegs graft with delivery pipe 9, solenoid valve 11 passes through threaded connection with delivery pipe 10, can carry the resin after the decomposition in the delivery pipe 10 through solenoid valve 11, support column 15 welds with reation kettle 12, operating panel 16 passes through screw connection with reation kettle 12, can control the device through operating panel 16.
As shown in fig. 1-3, in this embodiment, the water tank 2 is plugged with the decomposition tank 1, the first circulation pipe 3 is plugged with the decomposition tank 1, the second circulation pipe 4 is plugged with the decomposition tank 1, the water pump 5 is connected with the first circulation pipe 3 and the second circulation pipe 4 by screws, the electric heating pipe 6 is connected with the decomposition tank 1 by screws, and the decomposition tank 1 is connected with the console 7 by a clamping groove, so that not only can the silicone resin be continuously decomposed, and the water decomposition loss caused by the slow decomposition speed of the silicone resin be avoided, but also the silicone resin can be heated, the reaction efficiency caused by the low decomposition temperature of the silicone resin be avoided being low, and the working efficiency of the silicone resin continuous hydrolysis and condensation device is improved.
As shown in fig. 1-3, in this embodiment, the conveying pipe 10 is inserted into the reaction kettle 12, and the stirring shaft 14 is connected to the motor 13 through a key, so that the decomposed silicone resin can be stirred, thereby avoiding the poor reaction quality caused by the slow condensation efficiency of the decomposed silicone resin, and meeting the use requirement of the continuous hydrolysis and condensation device for silicone resin.
The specific implementation process of this embodiment is as follows: the device is powered on, organic silicon resin raw materials are poured into a decomposition tank 1, water is injected into the decomposition tank 1 through a water tank 2 to hydrolyze organic silicon resin, a water suction pump 5 is started through an operation panel 16, continuous circulating hydrolysis is respectively carried out from a first circulating pipe 3 and a second circulating pipe 4, a discharge valve is opened, the decomposed organic silicon resin is discharged into a conveying pipe 10, an electromagnetic valve 11 is started to convey the organic silicon resin into a reaction kettle 12, a motor 13 is started to rotate a stirring shaft 14 to stir the decomposed organic silicon resin and accelerate condensation of the organic silicon resin, the continuous hydrolysis and condensation device of the organic silicon resin is convenient to operate, and by arranging the first circulating pipe 3, the second circulating pipe 4, the decomposition tank 1 and an electric heating pipe 6, the continuous water decomposition of the organic silicon resin can be carried out, water decomposition loss caused by slow decomposition speed of the organic silicon resin is avoided, and the organic silicon can be heated, avoid the organic silicon resin decomposition temperature to cause the reaction efficiency low, improved the efficiency of the continuous condensation device that hydrolysises of organic silicon resin work, secondly, through setting up reation kettle 12, motor 13 and (mixing) shaft 14, can stir the organic silicon resin after the decomposition, avoid the organic silicon resin condensation efficiency after the decomposition to cause reaction quality poor slowly, satisfy the demand that the continuous condensation device that hydrolysises of organic silicon resin used.
The above-described embodiments are merely illustrative of the preferred embodiments of the present invention and are not intended to limit the spirit and scope of the present invention. Without departing from the design concept of the present invention, various modifications and improvements made by the technical solution of the present invention by those skilled in the art should fall into the protection scope of the present invention, and the technical contents claimed by the present invention have been fully recorded in the claims.
Claims (7)
1. A continuous hydrolysis and condensation device for organic silicon resin is characterized in that: including decomposition tank (1), electric heating pipe (6) and operation panel (7), decomposition tank (1) top is provided with water pitcher (2), water pitcher (2) below one side is provided with circulating pipe (3), circulating pipe (3) one side is provided with circulating pipe two (4), circulating pipe one (3) with circulating pipe two (4) top all is provided with suction pump (5), decomposition tank (1) inboard is provided with electric heating pipe (6), electric heating pipe (6) one side is provided with operation panel (7), water pitcher (2) with decomposition tank (1) are pegged graft, circulating pipe one (3) with decomposition tank (1) are pegged graft, circulating pipe two (4) with decomposition tank (1) are pegged graft, suction pump (5) with circulating pipe one (3) and circulating pipe two (4) all pass through the screw connection, the electric heating pipe (6) is connected with the decomposing tank (1) through screws, and the decomposing tank (1) is connected with the operating table (7) through clamping grooves.
2. The continuous hydrolysis and condensation device for silicone resin according to claim 1, wherein: frame columns (8) are arranged below the operating platform (7), and discharge pipes (9) are arranged between the frame columns (8).
3. The continuous hydrolysis and condensation device for silicone resin according to claim 2, wherein: delivery pipe (9) below is connected with conveyer pipe (10), conveyer pipe (10) middle part is provided with solenoid valve (11), solenoid valve (11) one side is provided with reation kettle (12), there is motor (13) reation kettle (12) top through the screw connection, motor (13) transmission output is connected with (mixing) shaft (14), (mixing) shaft (14) below is provided with support column (15), support column (15) top is provided with operating panel (16).
4. The continuous hydrolysis and condensation device for silicone resin according to claim 2, wherein: the frame column (8) is welded with the operating platform (7), the discharge pipe (9) is welded with the decomposition tank (1), and the first circulating pipe (3) and the second circulating pipe (4) are connected with the discharge pipe (9) in an inserted mode.
5. The continuous hydrolysis and condensation device for silicone resin according to claim 3, wherein: the delivery pipe (10) is connected with the discharge pipe (9) in an inserting mode, and the electromagnetic valve (11) is connected with the delivery pipe (10) through threads.
6. The continuous hydrolysis and condensation device for silicone resin according to claim 3, wherein: the conveying pipe (10) is connected with the reaction kettle (12) in an inserting mode, and the stirring shaft (14) is connected with the motor (13) through a key.
7. The continuous hydrolysis and condensation device for silicone resin according to claim 3, wherein: the support column (15) is welded with the reaction kettle (12), and the operation panel (16) is connected with the reaction kettle (12) through screws.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202120001892.2U CN214131610U (en) | 2021-01-04 | 2021-01-04 | Continuous hydrolysis and condensation device for organic silicon resin |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202120001892.2U CN214131610U (en) | 2021-01-04 | 2021-01-04 | Continuous hydrolysis and condensation device for organic silicon resin |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN214131610U true CN214131610U (en) | 2021-09-07 |
Family
ID=77547414
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202120001892.2U Expired - Fee Related CN214131610U (en) | 2021-01-04 | 2021-01-04 | Continuous hydrolysis and condensation device for organic silicon resin |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN214131610U (en) |
-
2021
- 2021-01-04 CN CN202120001892.2U patent/CN214131610U/en not_active Expired - Fee Related
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| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20210907 |
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| CF01 | Termination of patent right due to non-payment of annual fee |