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    • 11. 发明授权
    • Low temperature initiators for improving the rubber phase volume of HIPS formulations
    • 用于改善HIPS配方橡胶相体积的低温引发剂
    • US07754817B2
    • 2010-07-13
    • US11262641
    • 2005-10-31
    • Jose M. SosaShazia Ullah
    • Jose M. SosaShazia Ullah
    • C08F263/00C08F293/00
    • C08F279/02C08L51/04C08L2666/02
    • Peroxide initiators are disclosed that can be used at lower temperatures during HIPS production. Enhanced formation of graft polymers between polystyrene and polybutadiene (rubber) can be accomplished by using these lower temperature peroxide initiators that have a 1 hour half-life period at one or more temperatures from 95° C. to less than 111° C. during the pre-inversion stage. “Higher” temperature initiators are used during and/or after inversion. The use of such “low” temperature initiators improves polymerization rates and grafting values, while reducing the swell index and the amount of rubber used, thereby producing improved HIPS more rapidly and at a lower cost. Also disclosed are HIPS compositions and products produced by such “low” temperature initiators as well as a method of producing improved HIPS.
    • 公开了可以在HIPS生产期间在较低温度下使用的过氧化物引发剂。 在聚苯乙烯和聚丁二烯(橡胶)之间增强的接枝聚合物的形成可以通过使用这些低温过氧化物引发剂来实现,该引发剂在一个或多个温度从95℃到小于111℃的时间内具有1小时的半衰期 预转换阶段。 在反转期间和/或之后使用“较高”的温度引发剂。 使用这种“低”温度引发剂提高了聚合速率和接枝值,同时降低了溶胀指数和使用的橡胶的量,从而以更低的成本更快速地生产改进的HIPS。 还公开了由这种“低”温度引发剂生产的HIPS组合物和产物以及生产改进的HIPS的方法。
    • 18. 发明申请
    • Methods of Making High Impact Polystyrene
    • 制造高抗冲聚苯乙烯的方法
    • US20120108747A1
    • 2012-05-03
    • US13249383
    • 2011-09-30
    • Likuo SunJose M. SosaSerge EonCarlos CorletoScott Cooper
    • Likuo SunJose M. SosaSerge EonCarlos CorletoScott Cooper
    • C08F279/02C08F2/01
    • C08F2/001C08F212/08C08F279/02C08L9/06C08L2555/84
    • A process for producing high impact polystyrene including feeding at least one vinyl aromatic monomer, an elastomer, and a free radical initiator to a first linear flow reactor to form a reaction mixture. Polymerizing the reaction mixture in the first linear flow reactor to a point below the point at which phase inversion occurs to produce a first polymerization mixture and feeding the first polymerization mixture from the first linear flow reactor to a second linear flow reactor. Polymerizing the reaction mixture in the second linear flow reactor to at least a phase inversion point of the mixture to produce a second polymerization mixture and feeding the second polymerization mixture from the second linear flow reactor to at least a third linear flow reactor for post-inversion polymerization of the second polymerization mixture. The product stream can have an ESCR value of at least 10% toughness retained with less than 10 wt % rubber content.
    • 一种生产高抗冲聚苯乙烯的方法,包括将至少一种乙烯基芳族单体,弹性体和自由基引发剂进料至第一线性流动反应器以形成反应混合物。 将第一线性流动反应器中的反应混合物聚合到低于发生相转移点的点以产生第一聚合混合物并将第一聚合混合物从第一线性流动反应器进料到第二线性流动反应器。 将第二线性流动反应器中的反应混合物聚合到混合物的至少相转变点,以产生第二聚合混合物,并将第二聚合混合物从第二线性流动反应器进料到至少第三线性流动反应器用于后反转 第二聚合混合物的聚合。 产品流的ESCR值可以保持至少10%的韧性,橡胶含量小于10wt%。