CN205462172U - Silicone -acrylate emulsion production is with reation kettle's conduction oil system - Google Patents
Silicone -acrylate emulsion production is with reation kettle's conduction oil system Download PDFInfo
- Publication number
- CN205462172U CN205462172U CN201620103123.2U CN201620103123U CN205462172U CN 205462172 U CN205462172 U CN 205462172U CN 201620103123 U CN201620103123 U CN 201620103123U CN 205462172 U CN205462172 U CN 205462172U
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- China
- Prior art keywords
- feeding mechanism
- coil pipe
- cold oil
- deep fat
- oil feeding
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Abstract
The utility model discloses a silicone -acrylate emulsion production is with reation kettle's conduction oil system, including being used for setting up the first coil pipe in reation kettle, still include hot supply of oil device and cold oil feeding mechanism, the entry end of first coil pipe be connected to the export of hot supply of oil device and the export of cold oil feeding mechanism respectively through first three -way valve, the exit end of first coil pipe be connected to the entry of hot supply of oil device and the entry of cold oil feeding mechanism respectively through the second three -way valve, hot supply of oil device include first barrel and set up the second coil pipe in first barrel, the cold oil feeding mechanism include the second barrel and set up the cover that presss from both sides that being used for letting in subcooling salt solution in the second barrel outside, first coil pipe and first three -way valve between be equipped with the pump. The utility model aims at providing a control by temperature change is accurate, easy to operate's silicone -acrylate emulsion production is with reation kettle's conduction oil system.
Description
Technical field
This utility model relates to chemical production field, the heat-conducting oil system of a kind of silicone acrylic emulsion production reactor.
Background technology
The system that reaction temperature control accuracy and reaction temperature are higher, the heating of conduction oil and temperature are controlled to seem particularly
Important.In silicone acrylic emulsion, the raising for the temperature controlled accuracy of reaction system can significantly improve the qualified of product
Rate, reduces the operation easier of workman.
Utility model content
The purpose of this utility model is to provide the conduction oil system of a kind of temperature control silicone acrylic emulsion accurate, maneuverable production reactor
System.
The technical scheme that this utility model provides is: the heat-conducting oil system of a kind of silicone acrylic emulsion production reactor, including for setting
Put the first coil pipe in reactor, also include deep fat feeding mechanism and cold oil feeding mechanism, the arrival end of the first described coil pipe
Outlet and the outlet of cold oil feeding mechanism of deep fat feeding mechanism it is respectively connecting to by the first three-way valve, the first described coil pipe
The port of export is respectively connecting to entrance and the entrance of cold oil feeding mechanism of deep fat feeding mechanism, described deep fat by the second three-way valve
Feeding mechanism includes the first cylinder and the second coil pipe being arranged in the first cylinder, and described cold oil feeding mechanism includes the second cylinder
With the chuck for being passed through cool brine being arranged on outside the second cylinder, the entrance of described deep fat feeding mechanism is arranged on deep fat
The top of feeding mechanism, the outlet of described deep fat feeding mechanism is arranged on the bottom of deep fat feeding mechanism, described cold oil supply
The entrance of device is arranged on the top of cold oil feeding mechanism, and the outlet of described cold oil feeding mechanism is arranged on cold oil feeding mechanism
Bottom, is provided with pump between the first described coil pipe and the first three-way valve.
In the heat-conducting oil system of above-mentioned silicone acrylic emulsion production reactor, also include the expansion bucket of one and atmosphere, described
Expansion bucket be arranged on above the first coil pipe at 3-5 rice, described expand bucket by the top of the first connecting tube and the first cylinder even
Logical, the described bucket that expands is connected with the top of the second cylinder by the second connecting tube.
This utility model is after using technique scheme, and it has the beneficial effect that
(1) this programme use deep fat feeding mechanism and cold oil feeding mechanism to combine to improve this heat-conducting oil system anti-for temperature fluctuation
The agility of feedback and accuracy, specifically, in order to reduce apparatus processing difficulty and the accuracy for Temperature Feedback, for heat
Oil feeding mechanism uses coil pipe heating, uses chuck refrigeration for cold oil feeding mechanism, because coil pipe heating-up temperature feedback is quickly,
Chuck refrigeration difficulty of processing is low, considers and adds deep fat and the use frequency of cooling oil, uses above-mentioned setting to effectively reduce
Apparatus processing cost, and ensure that the accuracy of Temperature Feedback.
(2) this programme is safer in order to use, and is provided with expansion bucket, to equipment belt when can effectively prevent oil heat from expanding
The infringement come.
Accompanying drawing explanation
Fig. 1 is the structural representation of this utility model embodiment 1.
Detailed description of the invention
Below in conjunction with detailed description of the invention, the technical solution of the utility model is described in further detail, but does not constitute this
Any restriction of utility model.
Embodiment 1:
As it is shown in figure 1, the heat-conducting oil system of a kind of silicone acrylic emulsion production reactor, including in being arranged on reactor
One coil pipe 1, also includes deep fat feeding mechanism 2 and cold oil feeding mechanism 3, and the arrival end of the first described coil pipe 1 passes through the one or three
Logical valve 4 is respectively connecting to outlet and the outlet of cold oil feeding mechanism 3 of deep fat feeding mechanism 2, going out of the first described coil pipe 1
Mouth end is respectively connecting to entrance and the entrance of cold oil feeding mechanism 3 of deep fat feeding mechanism 2 by the second three-way valve 5, described
Deep fat feeding mechanism 2 include the first cylinder 21 and be arranged in the first cylinder 21 in heating the first cylinder 21 the of oil phase
Two coil pipes 22, described cold oil feeding mechanism 3 include the second cylinder 31 and be arranged on outside the second cylinder 31 for being passed through
The chuck 32 of cool brine, the entrance of described deep fat feeding mechanism 2 is arranged on the top of deep fat feeding mechanism 2, described deep fat
The outlet of feeding mechanism 2 is arranged on the bottom of deep fat feeding mechanism 2, and the entrance of described cold oil feeding mechanism 3 is arranged on cold oil
The top of feeding mechanism 3, the outlet of described cold oil feeding mechanism 3 is arranged on the bottom of cold oil feeding mechanism 3, described
It is provided with pump 9 between one coil pipe 1 and the first three-way valve 4.
In the present embodiment, this heat-conducting oil system also includes that the expansion bucket 6 of one and atmosphere, described expansion bucket 6 are arranged on
Above first coil pipe 1 at 3-5 rice, the described bucket 6 that expands is connected with the top of the first cylinder 21 by the first connecting tube 7, institute
The bucket 6 that expands stated is connected with the top of the second cylinder 31 by the second connecting tube 8.
In actual applications, when reactor starts to react, start pump 9, and the first three-way valve 4 is placed in the first coil pipe 1
The position connected with deep fat feeding mechanism 2, the second three-way valve 5 is placed in what the first coil pipe 1 was connected with deep fat feeding mechanism 2 simultaneously
Position, when reactor temperature is too high, can select the first three-way valve 4 is placed in the first coil pipe 1 and cold oil feeding mechanism 3
The position connected, the second three-way valve 5 is placed in the position that the first coil pipe 1 is connected with cold oil feeding mechanism 3 simultaneously.By above-mentioned behaviour
Having reached the purpose of accurate control reactor temperature, the most in actual applications, what the second coil pipe 22 was typically passed through is high pressure
The electrically heated mode that steam or the second coil pipe 22 use also can, use the mode of heating of coil pipe, the constant oil of oil phase can be improved
The control of temperature, the mode using chuck 32 to heat for cold oil feeding mechanism 3 can on the premise of ensureing cooling effect effectively
Reduce apparatus processing difficulty.
Above-described embodiment is this utility model preferably embodiment, but embodiment of the present utility model is not by above-described embodiment
Restriction, other any without departing from the change made under spirit of the present utility model and principle, modify, substitute, combine,
Simplify, all should be the substitute mode of equivalence, within being included in protection domain of the present utility model.
Claims (2)
1. a heat-conducting oil system for silicone acrylic emulsion production reactor, including the first coil pipe in being arranged on reactor, its
Being characterised by: also include deep fat feeding mechanism and cold oil feeding mechanism, the arrival end of the first described coil pipe passes through the first three-way valve
Being respectively connecting to outlet and the outlet of cold oil feeding mechanism of deep fat feeding mechanism, the port of export of the first described coil pipe passes through second
Three-way valve is respectively connecting to entrance and the entrance of cold oil feeding mechanism of deep fat feeding mechanism, and described deep fat feeding mechanism includes
One cylinder and the second coil pipe being arranged in the first cylinder, described cold oil feeding mechanism includes the second cylinder and is arranged on second
The chuck for being passed through cool brine of external side, the entrance of described deep fat feeding mechanism is arranged on the top of deep fat feeding mechanism,
The outlet of described deep fat feeding mechanism is arranged on the bottom of deep fat feeding mechanism, and the entrance of described cold oil feeding mechanism is arranged on
The top of cold oil feeding mechanism, the outlet of described cold oil feeding mechanism is arranged on the bottom of cold oil feeding mechanism, described first
It is provided with pump between coil pipe and the first three-way valve.
The heat-conducting oil system of silicone acrylic emulsion production reactor the most according to claim 1, it is characterised in that: also include one
With the expansion bucket of atmosphere, described expansion bucket is arranged on above the first coil pipe at 3-5 rice, and described expansion bucket passes through first
Connecting tube connects with the top of the first cylinder, and the described bucket that expands is connected with the top of the second cylinder by the second connecting tube.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620103123.2U CN205462172U (en) | 2016-02-01 | 2016-02-01 | Silicone -acrylate emulsion production is with reation kettle's conduction oil system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620103123.2U CN205462172U (en) | 2016-02-01 | 2016-02-01 | Silicone -acrylate emulsion production is with reation kettle's conduction oil system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205462172U true CN205462172U (en) | 2016-08-17 |
Family
ID=56673097
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620103123.2U Expired - Fee Related CN205462172U (en) | 2016-02-01 | 2016-02-01 | Silicone -acrylate emulsion production is with reation kettle's conduction oil system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205462172U (en) |
-
2016
- 2016-02-01 CN CN201620103123.2U patent/CN205462172U/en not_active Expired - Fee Related
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160817 Termination date: 20170201 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |