CN206549603U - A kind of reactor high-temp high-viscosity blowing attemperator - Google Patents
A kind of reactor high-temp high-viscosity blowing attemperator Download PDFInfo
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- CN206549603U CN206549603U CN201720214312.1U CN201720214312U CN206549603U CN 206549603 U CN206549603 U CN 206549603U CN 201720214312 U CN201720214312 U CN 201720214312U CN 206549603 U CN206549603 U CN 206549603U
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- conduction oil
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- blowing
- vomit pipe
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Abstract
The utility model provides a kind of reactor high-temp high-viscosity blowing attemperator, reactor is provided with heating jacket, there is conduction oil in heating jacket, conduction oil is heated by external device during the course of the reaction, makes conduction oil in heating jacket interior circulation, heat temperature raising effect is played, simultaneous reactions bottom end connects vomit pipe, there is the heat tracing pipe equipped with conduction oil, heat tracing pipe is S-type to be arranged in blowing pipe outer wall outside vomit pipe, complete coats vomit pipe;There is conduction oil to be connected by transfer valve and delivery valve with the heating jacket of reactor in heat tracing pipe, make heat conduction oil temperature in reactor consistent with heat conduction oil temperature in vomit pipe by control input valve and delivery valve;Reactor and vomit pipe use conduction oil interlayer structure, solve during polymerization blowing, because tube-cooled causes the process difficulties that drain hole is blocked, it is to avoid the risk that " production parking " is likely to occur.The blowing pipeline has quick-replaceable function, if vomit pipe replacing can be carried out in 30 minutes by occurring blocking, operational sequence is simple, does not influence production, reduces enterprise's production cost, improve utilization rate of equipment and installations.
Description
Technical field
The utility model belongs to chemical production equipment field, further there is provided a kind of reactor high-temp high-viscosity and puts
Attemperator is expected, for the discharging device of reactor in production processes of polyalcohol, mainly for high-temp high-viscosity material emptying mistake
The blowing pipeline heat insulation of journey, prevents the new device of blowing pipeline frozen plug.
Background technology
Polymer processing field, partial reaction needs to complete at high temperature, when polymerization was complete, and blowing process just seems outstanding
To be important, if the reduction of blowing temperature is too fast, material rapid condensation can be caused, drain hole is blocked so as to solidify.
In the prior art, it is ensured that drain hole is unimpeded following several method:Blowing is all ensured by dispensing speed first
Mouthful, substantially quick blowing is equally that system is anti-in field of polymer technology, during blowing to avoid drain hole congestion
The process answered, too fast blowing can cause material property to change, while the too fast pressure that can cause post processing of blowing is very big, it is right
Equipment for after-treatment has requirements at the higher level.Another discharging method is that by electrical heat tracing mode, but this method can cause reaction
The temperature difference of kettle and vomit pipe, part high molecular polymer performance during blowing can change.
In polymerization process, it is possible to the congestion of blowing link or failure occur, if material is not timely from reactor
Release, material final performance can be caused to change, therefore there must be alternative during blowing, i.e., with changeable
Material drain system, and the system possesses rapid exchange capabilities.
The content of the invention
The utility model provides a kind of reactor high-temp high-viscosity blowing attemperator, to solve existing polymer reaction
During blowing pipeline heat insulation problem, the device applied in polymerization workshop blowing link, and conduction oil companion is to blowing pipeline
Heat and jacket heat-preservation, it is to avoid high-temperature material solidifies during blowing, block blowing pipeline.Original fixed vomit pipe is designed to
Changeable type vomit pipe, which such as there is pipeline putty, in production to be changed in time, accomplished that easy to operate, production is stable, changed convenient
The features such as.
A kind of reactor high-temp high-viscosity blowing attemperator described in the utility model, including reactor, heating jacket,
Vomit pipe, heat tracing pipe, baiting valve, transfer valve, delivery valve;Wherein, reactor is provided with heating jacket, its heating jacket and had
Conduction oil, heats conduction oil by external device during the course of the reaction, makes conduction oil in heating jacket interior circulation, plays heating and rises
There is the heat tracing pipe equipped with conduction oil, the S-type row of heat tracing pipe outside temperature effect, simultaneous reactions bottom end connection vomit pipe, vomit pipe
Blowing pipe outer wall is listed in, complete coats vomit pipe;There is conduction oil to pass through transfer valve and delivery valve and reactor in heat tracing pipe
Heating jacket connection, heat conduction oil temperature is made in reactor with heat conduction oil temperature in vomit pipe by control input valve and delivery valve
Unanimously, it is ensured that be not in that cooling solidification blocks vomit pipe situation during blowing.
Good effect of the present utility model is:Reactor and vomit pipe use conduction oil interlayer structure, solve poly-
During symphysis production blowing, because tube-cooled causes the process difficulties that drain hole is blocked, it is to avoid " production parking " may go out
Existing risk.The blowing pipeline has quick-replaceable function, if vomit pipe replacing, behaviour can be carried out in 30 minutes by occurring blocking
Make process simple, do not influence production, reduce enterprise's production cost, improve utilization rate of equipment and installations.
Brief description of the drawings
Fig. 1 is the utility model structural representation;
In figure:1 reactor, 2 heating jackets, 3 vomit pipes, 4 heat tracing pipes, 5 baiting valves, 6 transfer valves, 7 delivery valves.
Embodiment
The one embodiment described in detail below in conjunction with accompanying drawing
As shown in figure 1, the utility model include reactor 1, it is heating jacket 2, vomit pipe 3, heat tracing pipe 4, baiting valve 5, defeated
Enter valve 6, delivery valve 7;The utility model during the course of the reaction, has conduction oil, in course of reaction in the heating jacket 2 of reactor 1
In by external device heat conduction oil, make conduction oil in the interior circulation of heating jacket 2, play heat temperature raising effect, simultaneous reactions
The bottom of kettle 1 connects vomit pipe 3, and vomit pipe 3 is outer to have the heat tracing pipe 4 equipped with conduction oil, and heat tracing pipe is stainless steel, according to S
Type is arranged in the outer wall of vomit pipe 3, and complete coats vomit pipe 3, and is wrapped up with insulation materials such as asbestos, plays insulation effect.Its
All heating media of middle heat tracing pipe 3 are that identical reaction kettle 1 heats the same conduction oils, in reactor bottom, have two transfer valves 6,
Delivery valve 7, makes in reactor 1 heat conduction oil temperature with heat conduction oil temperature one in vomit pipe 3 by transfer valve 6, the control of delivery valve 7
Cause, at the end of question response, open baiting valve 5, material is passed through and temperature of reaction kettle identical vomit pipe 3, it is smoothly flowed out
Vomit pipe 3.Be not in that cooling solidification blocks the situation of vomit pipe 3 during guarantee blowing.
The vomit pipe 3 also has quick-replaceable function, if being occurred in that during blowing, vomit pipe 3 is blocked.It can close immediately
Transfer valve 6, delivery valve 7 are closed, the bottom discharge valve 5 of reactor 1 is closed, quickly pulls down with heat tracing pipe 4, vomit pipe 3.Enable and carry
The standby vomit pipe 3 of heat tracing pipe 4, opens transfer valve 6, delivery valve 7 after installing, make conduction oil rapid in the interior circulation of heat tracing pipe 4
Heating, opens baiting valve 5, continues blowing.
Claims (2)
1. a kind of reactor high-temp high-viscosity blowing attemperator, it is characterised in that:
Including reactor, heating jacket, vomit pipe, heat tracing pipe, baiting valve, transfer valve, delivery valve;Wherein, reactor is provided with
There is conduction oil in heating jacket, heating jacket, conduction oil is heated by external device during the course of the reaction, make conduction oil in heating
Sheath interior circulation, play has equipped with conduction oil outside heat temperature raising effect, simultaneous reactions bottom end connection vomit pipe, vomit pipe
Heat tracing pipe, heat tracing pipe is S-type to be arranged in blowing pipe outer wall, and complete coats vomit pipe;There is conduction oil to pass through in heat tracing pipe defeated
Enter valve and delivery valve to connect with the heating jacket of reactor, heat conduction oil temperature in reactor is made by control input valve and delivery valve
It is consistent with heat conduction oil temperature in vomit pipe, it is ensured that to be not in that cooling solidification blocks vomit pipe situation during blowing.
2. a kind of reactor high-temp high-viscosity blowing attemperator according to claim 1, it is characterised in that:
The bottom of reactor is provided with baiting valve.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201720214312.1U CN206549603U (en) | 2017-03-07 | 2017-03-07 | A kind of reactor high-temp high-viscosity blowing attemperator |
Applications Claiming Priority (1)
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CN201720214312.1U CN206549603U (en) | 2017-03-07 | 2017-03-07 | A kind of reactor high-temp high-viscosity blowing attemperator |
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CN206549603U true CN206549603U (en) | 2017-10-13 |
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CN201720214312.1U Active CN206549603U (en) | 2017-03-07 | 2017-03-07 | A kind of reactor high-temp high-viscosity blowing attemperator |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108671577A (en) * | 2018-05-31 | 2018-10-19 | 山西豪仑科化工有限公司 | A kind of anthracene crystallization anti-clogging discharging device |
CN108864325A (en) * | 2018-08-10 | 2018-11-23 | 江苏富淼科技股份有限公司 | A kind of attemperator for belt polymerization |
CN112569865A (en) * | 2020-12-15 | 2021-03-30 | 安徽金禾实业股份有限公司 | Residue discharging device and method for maltol sublimation section |
CN114950314A (en) * | 2022-05-12 | 2022-08-30 | 博大东方新型化工(吉林)有限公司 | Discharging method and device used in PPC synthesis process |
-
2017
- 2017-03-07 CN CN201720214312.1U patent/CN206549603U/en active Active
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108671577A (en) * | 2018-05-31 | 2018-10-19 | 山西豪仑科化工有限公司 | A kind of anthracene crystallization anti-clogging discharging device |
CN108671577B (en) * | 2018-05-31 | 2020-12-08 | 山西豪仑科化工有限公司 | Anti-blocking discharging device for anthracene crystallization |
CN108864325A (en) * | 2018-08-10 | 2018-11-23 | 江苏富淼科技股份有限公司 | A kind of attemperator for belt polymerization |
CN108864325B (en) * | 2018-08-10 | 2023-06-09 | 江苏富淼科技股份有限公司 | Heat preservation device for belt polymerization |
CN112569865A (en) * | 2020-12-15 | 2021-03-30 | 安徽金禾实业股份有限公司 | Residue discharging device and method for maltol sublimation section |
CN114950314A (en) * | 2022-05-12 | 2022-08-30 | 博大东方新型化工(吉林)有限公司 | Discharging method and device used in PPC synthesis process |
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