CN203030275U - Solution polymerized styrene-butadiene rubber polyreactor - Google Patents
Solution polymerized styrene-butadiene rubber polyreactor Download PDFInfo
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- CN203030275U CN203030275U CN2012206933189U CN201220693318U CN203030275U CN 203030275 U CN203030275 U CN 203030275U CN 2012206933189 U CN2012206933189 U CN 2012206933189U CN 201220693318 U CN201220693318 U CN 201220693318U CN 203030275 U CN203030275 U CN 203030275U
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- pressure gauge
- thermometer
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- stirrer
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
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Abstract
A solution polymerized styrene-butadiene rubber polyreactor comprises a body, cooling tubes distributed on the inner periphery of the body, and a stirring shaft penetrating in the middle of the body. A variable frequency motor is connected to the upper portion of the stirring shaft through a reducer. A cooling jacket is further disposed in the body. The cooling tubes are divided into multiple groups, and each group of cooling tubes is disposed in a vertical retaining plate shape. The stirring shaft is provided with three stirrers from top to bottom, wherein the upper stirrer and the lower stirrer are turbine stirrers, and the middle stirrer is a pusher propeller stirrer. A thermometer, a pressure gauge and a feed pipeline are arranged at the top of the body, wherein the thermometer is a double-metal thermometer, the pressure gauge is a spring tube stainless steel pressure gauge or a diaphragm-seal pressure gauge or a diaphragm pressure gauge, and the feed pipeline is provided with a metal tube rotor flow meter. Compared with the prior art, the solution polymerized styrene-butadiene rubber polyreactor is simple in structure, reasonable in design and good in mass and heat transfer effect, uniformity and conversion rate of polyreaction are increased greatly, and product quality is improved.
Description
Technical field
The utility model relates to the chemical industry equipment field, is specially a kind of cohesion butadiene-styrene rubber polymerization reaction kettle.
Background technology
Along with China's rapid development of economy, living standards of the people improve constantly, and the domestic automobile industrial development is rapid, and auto industry has become one of pillar industry of China at present, country continues to improve the developing of automobile industry level, cultivates the consumption market based on the private consumption.China's automobile industry development planning is put into effect, and the policy of a series of stimulation automobile consumptions that match with it or is soon put into effect, and these all are conducive to guarantee increase in the year that keep about 10% in Chinese automobile market.The development of automobile industry will be conducive to increase domestic elastomeric demand.Butadiene-styrene rubber (SBR) is a kind of general purpose synthetic rubber that output is the highest in the world, consumption figure is maximum at present, wherein solution polymerized butadiene styrene rubber (SSBR) accounts for 7.01% of world's synthetic rubber total productive capacity, SSBR is in stage of steady development, and growth rate is very fast, is SBR development priority from now on.Solution polymerized butadiene styrene rubber (SSBR) is that butadiene and styrene adopt organolithium to cause anionic polymerisation in varsol and the copolymer that makes.Because advantages such as that it has is wear-resisting, cold-resistant, heat generation is low, color and luster good, ash content is few, purity is high and curingprocess rate is fast, very fast in developed country's development in recent years, along with popularizing of tire meridianization, especially the development of novel energy-conserving radial, tire is had higher requirement with glue, not only require the rubber strength height, anti-slippery is good, also requires flow resistance low.Solution polymerized butadiene styrene rubber has had the combination property that anti-slippery is good and resistance to rolling is low concurrently, it is the suitable sizing material of all-year tire, can satisfy tire at a high speed, safe, energy-conservation, comfortable requirement, tire drag with its manufacturing is low, wet-sliding resistant performance is good, anti-wear performance is good and living heat is low, has become to make radial-ply tyre and the requisite important source material of high-performance tire.The contents of ethylene of at present homemade SSBR is lower, performance indications such as wet-sliding resistant performance and resistance to rolling and steady quality performance and imported product still have gap, its main cause is the backwardness on technology and the equipment, usually contain alkynes, amine and other heavy ends such as present polymerisation with butadiene, if be directly used in the butadiene-styrene rubber polymerization, the conversion ratio of influence reaction and the quality of product.
The utility model content
The purpose of this utility model is exactly the defective that exists at prior art, and a kind of cohesion butadiene-styrene rubber polymerization reaction kettle is provided, and it can solve that existing butadiene contains impurity and the problem that influences the polymerisation effect.
The concrete technical scheme of the utility model is: comprise kettle and the inner cooling tubulation that distributes, the shaft that central authorities run through all around, shaft top connects variable-frequency motor by reductor; Also be provided with cooling jacket in the described kettle, described cooling tubulation is many groups respectively, and every group of cooling tubulation is arranged as the vertical bar baffle-like; Described shaft is provided with three agitators from top to bottom successively, and wherein upper and lower side is turbine agitator, the centre is pusher propeller formula agitator; The top of described kettle is provided with thermometer, Pressure gauge and feeding line, and wherein temperature is counted bimetallic thermometer, and Pressure gauge is bourdon tube stainless steel pressure table, diaphragm or diaphragm manometer, on the described feeding line metal-tube rotameter is installed.
Such scheme is more preferably: the volume of described reactor is 50m
3, body material is 16MnR.
The utility model compared with prior art, simple in structure, arrange rationally, mass-and heat-transfer is effective, improved the uniformity and the conversion ratio of polymerisation greatly, improved the quality of product.
Description of drawings
Fig. 1 is structural representation of the present utility model;
Among the figure: 1, variable-frequency motor, 2, reductor, 3, thermometer, 4, circulating water intake, 5, cooling jacket, 6, kettle, 7, cooling tubulation, 8, charging aperture, 9, flowmeter, 10, Pressure gauge, 11, circulating water outlet, 12, turbine agitator, 13, shaft, 14, pusher propeller formula agitator, 15, turbine agitator.
The specific embodiment
Below in conjunction with accompanying drawing the utility model is described further.
Referring to Fig. 1-2, comprise that volume is 50m
3, material be 16MnR kettle 6 and inner around the cooling tubulation 7, the shaft 13 that central authorities run through that distribute, shaft 13 tops connect variable-frequency motors 1 by reductor 2; Also be provided with cooling jacket 5 on the kettle 6, itself and cooling tubulation 7 common formation still internal cooling systems; Cooling tubulation 7 is many groups, and every group of cooling tubulation 7 is arranged as the vertical bar baffle-like, and be connected with circulating water outlet 11 with circulating water intake 4 respectively, the cooling tubulation group of vertical bar baffle-like can be used as mixing baffle and uses when playing cooling effect, improve the effect that mixes; Shaft 13 is provided with three agitators from top to bottom successively, wherein upper and lower side is the turbine agitator 12,15 that can cause radial flow of liquid, middle pusher propeller formula agitator 14 for causing axial liquid to flow, three agitators cooperatively interact, and realize the abundant mixing of internal flow; The top of kettle 6 is provided with thermometer 13, Pressure gauge 10 and charging aperture 8, and wherein thermometer 13 is bimetallic thermometer, and Pressure gauge 10 is bourdon tube stainless steel pressure table, diaphragm or diaphragm manometer, on the charging aperture 8 metal-tube rotameter is installed.
For those skilled in the art, under the prerequisite that does not break away from the utility model principle, might be to concrete size, perhaps partial structurtes are made some improvements and modifications, and these improvements and modifications also should be considered as protection domain of the present utility model.
Claims (2)
1. one kind is condensed the butadiene-styrene rubber polymerization reaction kettle, it is characterized in that: comprise kettle and the inner cooling tubulation that distributes, the shaft that central authorities run through all around, described shaft top connects variable-frequency motor by reductor; Also be provided with cooling jacket in the described kettle, described cooling tubulation is many groups respectively, and every group of cooling tubulation is arranged as the vertical bar baffle-like; Described shaft is provided with three agitators from top to bottom successively, and wherein upper and lower side is turbine agitator, the centre is pusher propeller formula agitator; The top of described kettle is provided with thermometer, Pressure gauge and feeding line, and wherein temperature is counted bimetallic thermometer, and Pressure gauge is bourdon tube stainless steel pressure table, diaphragm or diaphragm manometer, on the described feeding line metal-tube rotameter is installed.
2. cohesion butadiene-styrene rubber polymerization reaction kettle according to claim 1, it is characterized in that: the volume of described reactor is 50m
3, body material is 16MnR.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN2012206933189U CN203030275U (en) | 2012-12-16 | 2012-12-16 | Solution polymerized styrene-butadiene rubber polyreactor |
Applications Claiming Priority (1)
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CN2012206933189U CN203030275U (en) | 2012-12-16 | 2012-12-16 | Solution polymerized styrene-butadiene rubber polyreactor |
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CN203030275U true CN203030275U (en) | 2013-07-03 |
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CN2012206933189U Expired - Fee Related CN203030275U (en) | 2012-12-16 | 2012-12-16 | Solution polymerized styrene-butadiene rubber polyreactor |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104998573A (en) * | 2015-07-10 | 2015-10-28 | 常州市龙润机械有限公司 | Low-temperature stirring device and low-temperature stirring method |
CN108060370A (en) * | 2017-11-17 | 2018-05-22 | 马鞍山市海华金属制品有限公司 | A kind of temperature control type metal casting device |
CN110193332A (en) * | 2019-06-18 | 2019-09-03 | 南通金通储能动力新材料有限公司 | A kind of big volume ternary anode material precursor reaction kettle |
-
2012
- 2012-12-16 CN CN2012206933189U patent/CN203030275U/en not_active Expired - Fee Related
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104998573A (en) * | 2015-07-10 | 2015-10-28 | 常州市龙润机械有限公司 | Low-temperature stirring device and low-temperature stirring method |
CN108060370A (en) * | 2017-11-17 | 2018-05-22 | 马鞍山市海华金属制品有限公司 | A kind of temperature control type metal casting device |
CN110193332A (en) * | 2019-06-18 | 2019-09-03 | 南通金通储能动力新材料有限公司 | A kind of big volume ternary anode material precursor reaction kettle |
CN110193332B (en) * | 2019-06-18 | 2024-05-10 | 南通金通储能动力新材料有限公司 | Large-volume ternary anode material precursor reaction kettle |
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Legal Events
Date | Code | Title | Description |
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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: 20130703 Termination date: 20151216 |
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EXPY | Termination of patent right or utility model |