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Star high styrene rubber and preparation method thereof

A technology of high styrene rubber and styrene, applied in the field of star copolymer and its preparation, can solve the problems of insufficient tensile strength and hardness, low equipment utilization rate, high production cost, etc., to improve hardness and dynamic mechanical properties , Product performance is stable, the effect of improving rigidity

Active Publication Date: 2012-03-07
PETROCHINA CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] According to the search results, although there are many literatures and patents on the production of high-styrene rubber at home and abroad, most of them adopt latex coagulation technology. This process can obtain high-styrene rubber with better performance, but the main problem of this method is that : Firstly, in terms of technology, it is necessary to synthesize SBR-1500 or SBR-1502 latex and high-styrene resin emulsion respectively, and then mix the two emulsions that have passed the analysis in a certain proportion, and then obtain high-styrene rubber through coagulation and drying. The process flow is relatively long and requires two synthesis processes such as water phase, oil phase, initiator preparation and degassing; secondly, in terms of production cost, since the conversion rate of the synthetic SBR-1500 or SBR-1502 latex monomer is only 70%, there is no Reactive monomers account for 30%, and this part of monomers is difficult to recycle in small and medium-scale production devices, resulting in higher production costs and relatively more equipment, auxiliary materials, personnel, time, and energy required for the polymerization process; In terms of production cycle, since the synthesis temperature of high-styrene resin emulsion is high-temperature polymerization, there are many structural gels in the polymerization kettle, and the polymerization kettle used usually needs to be cleaned once for 10 batches of production, so the equipment utilization rate is low
The above-mentioned polymers all have the disadvantages that the tensile strength and hardness of the product are not high enough

Method used

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  • Star high styrene rubber and preparation method thereof

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Experimental program
Comparison scheme
Effect test

Embodiment 1

[0029] In a jacketed 15L stainless steel reactor, the system was replaced 3 times with argon. In the polymerization kettle, add 4315g of cyclohexane, 420g of styrene (accounting for 35% of the total amount of monomers), 280g of butadiene (accounting for 23.3% of the total amount of monomers), add 12.1mmol of n-butyllithium, be warming up to 50°C, polymerize for 80min, then press the mixture of 4.32g THF, 2194g cyclohexane, 300g styrene (25% of the total monomer), 200g butadiene (16.7% of the total monomer) into polymerization The kettle continued to react for 60min, and the monomer was heated to 70°C after complete conversion, and 3.3mmolSncl was added. 4 The coupling agent is used for coupling reaction, and the reaction time is 60 min. After the coupling reaction is completed, the coupled reaction mixture is treated with water, 100 g of water, 12 g of antioxidant 1010 [tetra-(4-hydroxy-3,5-tert-butylphenylpropionic acid) pentaerythritol ester] are added, and the mixture is s...

Embodiment 2

[0033] In a jacketed 15L stainless steel reactor, the system was replaced 3 times with argon. In the polymerization kettle, add cyclohexane 4444g, styrene 330g (accounting for 27.5% of the total monomer), butadiene 300g (accounting for 25% of the total monomer), accurately add 24.1mmol of n-butyllithium, and heat up. to 60°C, polymerize for 50min, and then press the mixture of 8.64g THF, 2088g cyclohexane, 330g styrene (accounting for 27.5% of the total monomer), 240g butadiene (accounting for 20% of the total monomer) into The polymerization kettle continued to react for 70min. After the monomer was completely converted, the temperature was raised to 80°C, and 6.6mmolSncl was added in two times. 4 (The first time to join Sncl 4 80% of the total amount, the remaining 20% ​​of the coupling agent was added after the reaction for 15 min to carry out the coupling reaction, and the reaction time was 80 min. After the coupling reaction was completed, the coupled reaction mixture w...

Embodiment 3

[0037] In a jacketed 15L stainless steel reactor, the system was replaced 3 times with argon. In the polymerization kettle, add cyclohexane 2044g, styrene 324g (accounting for 27% of the total monomer), butadiene 396g (accounting for 33% of the total monomer), add 8.1mmol of n-butyllithium, be warming up to 60 ℃, polymerize for 50min, then press the mixture of 2.16g THF, 3777g cyclohexane, 216g (accounting for 18% of the total monomer) styrene, 264g (accounting for 22% of the total monomer) butadiene into polymerization The kettle continued to react for 70min. After the monomer was completely converted, it was heated to 80°C, and 2.2mmolSncl was added in two times. 4 (The first time to join Sncl 4 80% of the total amount, the remaining 20% ​​of the coupling agent was added after the reaction for 15 min to carry out the coupling reaction, and the reaction time was 80 min. After the coupling reaction is completed, the coupled reaction mixture is treated with water, and 10 g of...

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Abstract

The invention provides star high styrene rubber and a preparation method thereof, and the star high styrene rubber has a structural formula as follows: Y-[B1->S1-B2 / S2]4, wherein Y is Si or Sn; B1->S1 is polystyrene or polybutadiene tapered block copolymer; B2 / S2 is polystyrene or polybutadiene random copolymer; in the structural formula, the polystyrene or polybutadiene tapered block is 40-75wt%, and the mass fraction of the polystyrene or polybutadiene random copolymer is 25-60wt%; and in the star high styrene rubber copolymer, the styrene content is 45-75wt% and the butadiene content is 25-55wt%.The preparation method of the star high styrene rubber is as follows: adding an initiator once, adding monomers in a polymerization system at twice in a sequence, and then adding a coupler for coupling reaction after the polymerization to obtain the star high styrene rubber. The high styrene rubber in the invention has the characteristics of high hardness and good strength, can improve properties of rigidity, hardness and wearing resistance and lower contraction rate of the rubber products when being used with various synthesized rubber or natural rubber together, and can be widely usedin shoemaking industry, tyre industry, printing industry and other industries.

Description

technical field [0001] The invention relates to a star-shaped copolymer and a preparation method thereof, in particular to a star-shaped high styrene rubber with high rigidity, high hardness and high wear resistance and a preparation method thereof. Background technique [0002] A copolymer composed of butadiene and styrene, if combined with a high styrene content, will obtain a resin copolymer with low elasticity and high plasticity; otherwise, a rubber-like copolymer with high elasticity and low plasticity will be obtained. Usually, the copolymer with styrene binding amount in the molecular structure between 45% and 70% is called high styrene rubber. The notable characteristics of high styrene rubber are its high hardness, good strength, and physical properties of rubber. When used in combination with various synthetic rubbers or natural rubbers, it can improve the rigidity, hardness, wear resistance, and reduce shrinkage of rubber products. It can be widely used in the s...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C08F297/04C08F2/38C08F8/42
Inventor 胡才仲董静康安福陶惠平陈红宋同江史工昌王振华龚光碧梁滔李锦山汤海鲲吕红杨绮波怀惠珍周漫
Owner PETROCHINA CO LTD
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