CN205088170U - Synthetic cauldron tail gas line of vinyl resin improves device - Google Patents
Synthetic cauldron tail gas line of vinyl resin improves device Download PDFInfo
- Publication number
- CN205088170U CN205088170U CN201520841297.4U CN201520841297U CN205088170U CN 205088170 U CN205088170 U CN 205088170U CN 201520841297 U CN201520841297 U CN 201520841297U CN 205088170 U CN205088170 U CN 205088170U
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- CN
- China
- Prior art keywords
- vinylite
- vinyl resin
- synthesis reactor
- valve
- tail gas
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Abstract
The utility model relates to a vinyl resin field, concretely relates to synthetic cauldron tail gas line of vinyl resin improves device, it includes the synthetic cauldron of vinyl resin, the synthetic cauldron of epoxy, the three -way valve, the buffer tank, the tail gas system, still include the governing valve, the waste gas collecting system, the gate valve, the flange, the side line of leaving a tail gas treatment in the cauldron junction is synthesized in the adoption at the vinyl resin, it is direct with exhaust gas collection to waste gas collecting system, increase ordinary unsaturated polyester resins reation kettle production vinyl resin function, reduce and wash the cost, and thoroughly separate vinyl resin production technology and epoxy production technology, stop two kinds of products and put the mutual interference after the switching into production, improve equipment service function, the turning apparatus is simple in structure, and convenient for operation, possesses good practicality.
Description
Technical field
The utility model relates to Vinylite field, is specifically related to a kind of Vinylite synthesis reactor exhaust gas line modifying device.
Background technology
Vinylite, English name, also known as VinylEsterResins, is internationally recognized height corrosion-resistant resin.Vinyl ester polyester resin is a kind of unsaturated polyester resin being dissolved in vinylbenzene liquid and containing the special construction of unsaturated double-bond, vinyl ester polyester resin has good corrosion resisting property, be better than metaphenylene unsaturated polyester, mechanical property is suitable with standard type epoxy vingl ester resin, especially fatigue performance and dynamic load performance; In addition, comparatively resins for universal use, vinyl ester polyester resin has again good weather resistance, and VPR vinyl ester polyester resin has again good glass wetting property and processing performance simultaneously, be suitable for various FRP moulding process, comprise the various composite technologys such as Filament-wound Machine, pultrusion, hand paste, injection.
In Vinylite production technique, there is technique hidden danger when changing with epoxy resin, the free acid in Vinylite production can pollute the production of epoxy resin, reduces quality product.
Utility model content
The purpose of this utility model is defect for prior art and deficiency, there is provided a kind of structure simple, reasonable in design, a kind of Vinylite synthesis reactor exhaust gas line modifying device easy to use, it adopts the side line outputing a vent gas treatment in Vinylite synthesis reactor junction, directly by exhaust collection to waste gas collecting system, increase common unsaturated polyester reactor and produce Vinylite function, reduce cleaning cost, and thoroughly Vinylite production technique and epoxy resin production technique are separated, stop two kinds of products and produce the mutual interference after switching, improve equipment use function, this utility model structure is simple, easy to operate, possesses good practicality.
For achieving the above object, the technical solution adopted in the utility model is:
A kind of Vinylite synthesis reactor exhaust gas line modifying device described in the utility model, comprise Vinylite synthesis reactor, epoxy resin synthesis reactor, T-valve, surge tank, exhaust system, also comprise variable valve, waste gas collecting system, gate valve, flange, described Vinylite synthesis reactor, surge tank, variable valve and exhaust system adopt pipeline to be connected, described T-valve is arranged on the pipeline between surge tank and Vinylite synthesis reactor, described variable valve is arranged on the outer top of epoxy resin synthesis reactor, described Vinylite synthesis reactor, flange, gate valve and waste gas collecting system adopt pipeline to be connected, described Flange joint is at Vinylite synthesis reactor exit end, after described gate valve is connected to flange, before waste gas collecting system.
Further, installation process tank between described waste gas collecting system and gate valve.
Again further, described treatment tank is alkalescence or neutral.
After adopting said structure, the utility model beneficial effect is:
1. Vinylite production technique and epoxy resin production technique are thoroughly isolated by this utility model, stopped two kinds of products switch aborning after interfere with each other, achieve a production line and produce two kinds of different resins products simultaneously.
2. this utility model improves the using function of equipment, also improves the throughput of equipment to Vinylite, also ensure that the quality product of epoxy resin simultaneously, decrease cleaning cost.
3. the quality of product obtains significant raising, and stability is greatly improved, and shortens production cycle and production switch cycle, reduces cost, bring good economic benefit.
4. this utility model structurally has simply, the features such as feasibility is strong, operationally extremely simple again, therefore this utility model has possessed good practicality, has and implement necessity greatly in Vinylite synthesis technique.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model;
Description of reference numerals:
1, Vinylite synthesis reactor; 2, epoxy resin synthesis reactor; 3, T-valve; 4, surge tank; 5, variable valve; 6, exhaust system; 7, waste gas collecting system; 8, flange; 9, gate valve; 10, treatment tank.
Embodiment
Below in conjunction with accompanying drawing, the utility model is further described.
As shown in Figure 1, a kind of Vinylite synthesis reactor exhaust gas line modifying device described in the utility model, comprise Vinylite synthesis reactor 1, epoxy resin synthesis reactor 2, T-valve 3, surge tank 4, exhaust system 6, also comprise variable valve 5, waste gas collecting system 7, gate valve 9, flange 8, described Vinylite synthesis reactor 1, surge tank 4, variable valve 5 adopts pipeline to be connected with exhaust system 6, described T-valve 3 is arranged on the pipeline between surge tank 4 and Vinylite synthesis reactor 1, described variable valve 5 is arranged on the outer top of epoxy resin synthesis reactor 2, described Vinylite synthesis reactor 1, flange 8, gate valve 9 adopts pipeline to be connected with waste gas collecting system 7, described flange 8 is connected to the exit end of Vinylite synthesis reactor 1, after described gate valve 9 is connected to flange 8, before waste gas collecting system 7.
Further, installation process tank 10 between described waste gas collecting system 7 and gate valve 9.
Again further, described treatment tank 10 is alkalescence or neutral.
The utility model in use, the break-make of T-valve controls the switching between Vinylite synthesis reactor and epoxy resin synthesis reactor, the discharge of tail gas in epoxy resin synthesis reactor is determined by variable valve, and the exhaust emissions of Vinylite synthesis reactor is controlled by flange and gate valve, and have treatment tank for the free acid collection and treatment in still, residual gas is drained into waste gas collecting system.Stop free acid in Vinylite synthesis technique like this to the impact of product in epoxy resin synthesis reactor.
Vinylite production technique and epoxy resin production technique are isolated by this utility model, stopped two kinds of products switch aborning after interfere with each other, achieve a production line and produce two kinds of different resins products simultaneously, improve the using function of equipment, equipment improves to the throughput of Vinylite also tool simultaneously, also ensure that the quality product of epoxy resin simultaneously, decrease cleaning cost.In use, the quality of product obtains significant raising to this utility model, and stability is greatly improved, and shortens production cycle and production switch cycle, reduces cost, bring good economic benefit.This utility model structurally has simply, the features such as feasibility is strong, operationally extremely simple again, therefore this utility model has possessed good practicality, has and implement necessity greatly in Vinylite synthesis technique.
The above is only better embodiment of the present utility model, therefore all equivalences done according to structure, feature and the principle described in the utility model patent claim change or modify, and are included in the utility model patent claim.
Claims (3)
1. a Vinylite synthesis reactor exhaust gas line modifying device, comprise Vinylite synthesis reactor (1), epoxy resin synthesis reactor (2), T-valve (3), surge tank (4), exhaust system (6), it is characterized in that, also comprise variable valve (5), waste gas collecting system (7), gate valve (9), flange (8), described Vinylite synthesis reactor (1), surge tank (4), variable valve (5) and exhaust system (6) adopt pipeline to be connected, described T-valve (3) is arranged on the pipeline between surge tank (4) and Vinylite synthesis reactor (1), described variable valve (5) is arranged on the outer top of epoxy resin synthesis reactor (1), described Vinylite synthesis reactor (1), flange (8), gate valve (9) and waste gas collecting system (7) adopt pipeline to be connected, described flange (8) is connected to the exit end of Vinylite synthesis reactor (1), after described gate valve (9) is connected to flange (8), before waste gas collecting system (7).
2. a kind of Vinylite synthesis reactor exhaust gas line modifying device according to claims 1, is characterized in that, installation process tank (10) between described waste gas collecting system (7) and gate valve (9).
3. a kind of Vinylite synthesis reactor exhaust gas line modifying device according to claims 2, is characterized in that, described treatment tank (10) is alkalescence or neutral.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520841297.4U CN205088170U (en) | 2015-10-28 | 2015-10-28 | Synthetic cauldron tail gas line of vinyl resin improves device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520841297.4U CN205088170U (en) | 2015-10-28 | 2015-10-28 | Synthetic cauldron tail gas line of vinyl resin improves device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205088170U true CN205088170U (en) | 2016-03-16 |
Family
ID=55478875
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520841297.4U Expired - Fee Related CN205088170U (en) | 2015-10-28 | 2015-10-28 | Synthetic cauldron tail gas line of vinyl resin improves device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205088170U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108559078A (en) * | 2018-06-12 | 2018-09-21 | 江苏海阳锦纶新材料有限公司 | A kind of low melting point PA6/66 continuous production devices and production method |
-
2015
- 2015-10-28 CN CN201520841297.4U patent/CN205088170U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108559078A (en) * | 2018-06-12 | 2018-09-21 | 江苏海阳锦纶新材料有限公司 | A kind of low melting point PA6/66 continuous production devices and production method |
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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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160316 Termination date: 20171028 |