CN109954458A - Resin continuous production device - Google Patents
Resin continuous production device Download PDFInfo
- Publication number
- CN109954458A CN109954458A CN201711428249.2A CN201711428249A CN109954458A CN 109954458 A CN109954458 A CN 109954458A CN 201711428249 A CN201711428249 A CN 201711428249A CN 109954458 A CN109954458 A CN 109954458A
- Authority
- CN
- China
- Prior art keywords
- compound
- reaction kettle
- compound material
- heat preservation
- feed pipe
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 238000010924 continuous production Methods 0.000 title claims abstract description 13
- 239000011347 resin Substances 0.000 title claims abstract description 11
- 229920005989 resin Polymers 0.000 title claims abstract description 11
- 239000000463 material Substances 0.000 claims abstract description 38
- 238000006243 chemical reaction Methods 0.000 claims abstract description 34
- 150000001875 compounds Chemical class 0.000 claims abstract description 30
- 238000003860 storage Methods 0.000 claims abstract description 23
- 238000004321 preservation Methods 0.000 claims abstract description 22
- 238000010438 heat treatment Methods 0.000 claims abstract description 5
- 238000004519 manufacturing process Methods 0.000 description 7
- 238000005580 one pot reaction Methods 0.000 description 4
- 238000009413 insulation Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000000151 deposition Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00002—Chemical plants
- B01J2219/00027—Process aspects
- B01J2219/00033—Continuous processes
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Other Resins Obtained By Reactions Not Involving Carbon-To-Carbon Unsaturated Bonds (AREA)
Abstract
The present invention relates to resin continuous production devices, including reaction kettle, react kettle cover, compound material material-compound tank, keep the temperature storage still, the reaction kettle is equipped with heating collet, bottom is equipped with discharge port, connect general pipeline, general pipeline is equipped with multiple branch pipes, each branch pipe is connected with corresponding heat preservation storage still, the reaction kettle cover side and compound material material-compound tank are equipped with multiple single material feeding tubes, there is compound material feed pipe in the reaction kettle cover other side, the compound material feed pipe is connect with compound material material-compound tank, the single material feeding tube and compound material feed pipe are equipped with flow pump, control signal on flow pump is connect with controller, compound material material-compound tank is equipped with sample tap.The present apparatus allows continuous production.
Description
Technical field
The invention belongs to production of resins manufacture fields, and in particular to resin continuous production device.
Background technique
The master operation of production of resins is synthetic reaction in a kettle, is carried out at certain temperature and pressure condition,
It needs to react in a certain temperature conditions during General reactions for a long time.If waiting reaction to terminate in a kettle,
Start to produce next time after discharging again, the time is long, and yield is few.
Summary of the invention
Goal of the invention: purpose of the invention is to overcome the shortcomings in the prior art, provides a kind of resin continuous production
Device.
Technical solution: in order to solve the above-mentioned technical problem, resin continuous production device of the present invention, including reaction
Kettle, reaction kettle cover, compound material material-compound tank, heat preservation storage still, the reaction kettle are equipped with heating collet, and bottom is equipped with discharge port,
Connect general pipeline, general pipeline is equipped with multiple branch pipes, and each branch pipe connects with corresponding heat preservation storage still, the reaction kettle cover side and
Compound material material-compound tank is equipped with multiple single material feeding tubes, and there are compound material feed pipe, institute in the reaction kettle cover other side
It states compound material feed pipe to connect with compound material material-compound tank, the single material feeding tube is equipped with compound material feed pipe
Flow pump, the control signal on flow pump are connect with controller, and compound material material-compound tank is equipped with sample tap.
The branch pipe of the heat preservation storage still is equipped with switch valve, and the control signal of switch valve is connect with controller, one pot reaction
Enter a heat preservation storage still after kettle production, the switch valve on the heat preservation storage still branch pipe is opened, and rest switch valve is closed, another
Enter another heat preservation storage still after pot reaction kettle production, the switch valve on the heat preservation storage still branch pipe is opened, rest switch valve
It closes, such continuous production.
The utility model has the advantages that compared with prior art, the present invention in a kettle realize preamble reaction after, into heat preservation storage still
Insulation reaction is carried out, reaction kettle can be produced next time, and it enters back into another heat preservation storage still and carries out insulation reaction, such as
Preamble reaction needs 5 hours, and insulation reaction needs 25 hours, that can configure 5 heat preservation storage stills, and reaction kettle can be with every 5 hours
One pot of reaction, continuous production not so can only be 30 one pot of hour.
Detailed description of the invention
Fig. 1 is structural schematic diagram of the invention.
In figure: 1, reaction kettle, 2, reaction kettle cover, 3, compound material material-compound tank, 4, heat preservation storage still, 5, heating collet, 6,
Discharge port, 7, general pipeline, 8, branch pipe, 9, single material feeding tube, 10, compound material feed pipe, 11, flow pump, 12, controller,
13, sample tap, 14, switch valve.
Specific embodiment
The present invention is further illustrated with reference to the accompanying drawings and examples.
As shown in Figure 1, resin continuous production device, including reaction kettle 1, reaction kettle cover 2, compound material material-compound tank 3, heat preservation
Storage still 4, the reaction kettle 1 are equipped with heating collet 5, and bottom is equipped with discharge port 6, connect general pipeline 7, and general pipeline 7 is equipped with multiple
Pipe 8, each branch pipe 8 are connected with corresponding heat preservation storage still 4, and 2 side of reaction kettle cover is equipped with compound material material-compound tank 3
There are compound material feed pipe 10, the compound material feed pipe in multiple single material feeding tubes 9, reaction 2 other side of kettle cover
10 connect with compound material material-compound tank 3, and the single material feeding tube 9 is equipped with flow pump 11 with compound material feed pipe 10,
Control signal on flow pump 11 is connect with controller 12, and compound material material-compound tank 3 is equipped with sample tap 13, the heat preservation storage
The branch pipe for depositing kettle is equipped with switch valve 14, and the control signal of switch valve 14 is connect with controller 12, enters after the production of one pot reaction kettle
One heat preservation storage still, the switch valve on the heat preservation storage still branch pipe are opened, and rest switch valve is closed, another pot of reaction kettle production
Enter another heat preservation storage still afterwards, the switch valve on the heat preservation storage still branch pipe is opened, and rest switch valve is closed, so continuous
Production.
The present invention provides a kind of thinking and methods, and there are many method and the approach for implementing the technical solution, the above institute
Stating is only the preferred embodiment of the present invention, it is noted that for those skilled in the art, is not being departed from
Under the premise of the principle of the invention, several improvements and modifications can also be made, these improvements and modifications also should be regarded as guarantor of the invention
Range is protected, all undefined components in this embodiment can be implemented in the prior art.
Claims (2)
1. resin continuous production device, including reaction kettle, reaction kettle cover, compound material material-compound tank, heat preservation storage still, feature exist
In: the reaction kettle is equipped with heating collet, and bottom is equipped with discharge port, connects general pipeline, and general pipeline is equipped with multiple branch pipes, each branch pipe
It is connected with corresponding heat preservation storage still, the reaction kettle cover side and compound material material-compound tank are equipped with multiple single feedstocks
There are compound material feed pipe in pipe, the reaction kettle cover other side, and the compound material feed pipe is connect with compound material material-compound tank,
The single material feeding tube and compound material feed pipe are equipped with flow pump, and the control signal on flow pump connects with controller
It connects, compound material material-compound tank is equipped with sample tap.
2. resin continuous production device according to claim 1, it is characterised in that: the branch pipe of the heat preservation storage still is equipped with
The control signal of switch valve, switch valve is connect with controller.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201711428249.2A CN109954458A (en) | 2017-12-26 | 2017-12-26 | Resin continuous production device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201711428249.2A CN109954458A (en) | 2017-12-26 | 2017-12-26 | Resin continuous production device |
Publications (1)
Publication Number | Publication Date |
---|---|
CN109954458A true CN109954458A (en) | 2019-07-02 |
Family
ID=67021664
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201711428249.2A Pending CN109954458A (en) | 2017-12-26 | 2017-12-26 | Resin continuous production device |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN109954458A (en) |
Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN201288158Y (en) * | 2008-11-14 | 2009-08-12 | 南京科盛环保科技有限公司 | Multi-kettle charge full-automatic continuous production apparatus |
CN203342755U (en) * | 2013-06-24 | 2013-12-18 | 江苏德峰药业有限公司 | Discharging device of high-pressure kettle |
WO2015139526A1 (en) * | 2014-03-17 | 2015-09-24 | 江苏华东锂电技术研究院有限公司 | Device for continuously preparing lithium iron phosphate |
CN205838902U (en) * | 2016-04-07 | 2016-12-28 | 无锡华通沥青新技术发展有限公司 | A kind of continuous modified asphalt production system |
CN106548818A (en) * | 2015-09-16 | 2017-03-29 | 中国辐射防护研究院 | A kind of on-radiation simulation concentrated solution preparing process and special purpose device |
CN206121655U (en) * | 2016-08-29 | 2017-04-26 | 湖北犇星农化有限责任公司 | A device for automizing prepare chlopyrifos milk oil preparation |
CN206355986U (en) * | 2016-12-30 | 2017-07-28 | 重庆喜旋生物科技有限公司 | A kind of material-compound tank be easy to sample and observed |
CN207872132U (en) * | 2017-12-26 | 2018-09-18 | 宜兴市兴南复合材料厂有限公司 | resin continuous production device |
-
2017
- 2017-12-26 CN CN201711428249.2A patent/CN109954458A/en active Pending
Patent Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN201288158Y (en) * | 2008-11-14 | 2009-08-12 | 南京科盛环保科技有限公司 | Multi-kettle charge full-automatic continuous production apparatus |
CN203342755U (en) * | 2013-06-24 | 2013-12-18 | 江苏德峰药业有限公司 | Discharging device of high-pressure kettle |
WO2015139526A1 (en) * | 2014-03-17 | 2015-09-24 | 江苏华东锂电技术研究院有限公司 | Device for continuously preparing lithium iron phosphate |
CN106548818A (en) * | 2015-09-16 | 2017-03-29 | 中国辐射防护研究院 | A kind of on-radiation simulation concentrated solution preparing process and special purpose device |
CN205838902U (en) * | 2016-04-07 | 2016-12-28 | 无锡华通沥青新技术发展有限公司 | A kind of continuous modified asphalt production system |
CN206121655U (en) * | 2016-08-29 | 2017-04-26 | 湖北犇星农化有限责任公司 | A device for automizing prepare chlopyrifos milk oil preparation |
CN206355986U (en) * | 2016-12-30 | 2017-07-28 | 重庆喜旋生物科技有限公司 | A kind of material-compound tank be easy to sample and observed |
CN207872132U (en) * | 2017-12-26 | 2018-09-18 | 宜兴市兴南复合材料厂有限公司 | resin continuous production device |
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PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
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WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20190702 |