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    • 6. 发明授权
    • Extrusion method for making polycarbonate
    • 制造聚碳酸酯的挤出方法
    • US06506871B1
    • 2003-01-14
    • US10167903
    • 2002-06-12
    • Norberto SilviPatrick Joseph McCloskeyJames DayMark Howard Giammattei
    • Norberto SilviPatrick Joseph McCloskeyJames DayMark Howard Giammattei
    • C08G6400
    • C08G64/307
    • Extrusion of a mixture of an ester-substituted diaryl carbonate, such as bis(methyl salicyl) carbonate, a dihydroxy aromatic compound such as bisphenol A and a transesterification catalyst such as tetrabutylphosphonium acetate (TBPA) affords polycarbonate having a weight average molecular weight of greater than 20,000 daltons. The extruder is equipped with one or more vacuum vents to remove by-product ester-substituted phenol. Similarly, a precursor polycarbonate having ester-substituted phenoxy endgroups, for example methyl salicyl endgroups, when subjected to extrusion affords a polycarbonate having a significantly increased molecular weight relative to the precursor polycarbonate. The reaction to form a higher molecular weight polycarbonate may be catalyzed by residual transesterification catalyst present in the precursor polycarbonate, or by a combination of any residual catalyst and an additional catalyst such as TBPA introduced in the extrusion step. Fries rearrangement products are not observed in the product polycarbonates.
    • 碳酸二(甲基水杨基)酯,二羟基芳族化合物如双酚A和酯交换催化剂如四丁基鏻乙酸酯(TBPA)的酯取代的二芳基碳酸酯的混合物的挤出得到重均分子量更大的聚碳酸酯 超过20,000道尔顿。 挤出机配备有一个或多个真空通风口以除去副产物酯取代的苯酚。 类似地,具有酯取代的苯氧基端基的前体聚碳酸酯,例如甲基水杨基端基,当进行挤出时,得到相对于前体聚碳酸酯具有显着增加的分子量的聚碳酸酯。 形成较高分子量聚碳酸酯的反应可以通过存在于前体聚碳酸酯中的残留酯交换催化剂,或者通过任何残余催化剂和另外的催化剂如在挤出步骤中引入的TBPA的组合来催化。 在产品聚碳酸酯中没有观察到薯条重排产物。
    • 7. 发明授权
    • Method for preparing a polycarbonate oligomer mixture at low temperature for manufacturing polycarbonate
    • 低温制备聚碳酸酯低聚物混合物制造聚碳酸酯的方法
    • US07041775B2
    • 2006-05-09
    • US10830163
    • 2004-04-21
    • Maria Tomas MartinezAlberto NisoliAlfredo Lopez CarreteroGanesh KailasamDavid DomingoPatrick Joseph McCloskey
    • Maria Tomas MartinezAlberto NisoliAlfredo Lopez CarreteroGanesh KailasamDavid DomingoPatrick Joseph McCloskey
    • C08G64/00
    • C08G64/307B01J19/18B01J19/1806B01J19/1887B01J19/20B01J2219/00031B01J2219/0004B01J2219/00083B01J2219/00094B01J2219/00166B01J2219/00184B01J2219/00186C08G64/205
    • The present invention provides a method of making polycarbonate oligomers, polycarbonate, molded articles formed from polycarbonate, and an apparatus for making polycarbonate. An oligomer mixture is first prepared by the steps of providing an equilibration system comprising a vessel, a reaction mixture contained within the vessel, and means for mixing the reaction mixture contained within the vessel wherein the reaction mixture comprises a melted activated diaryl carbonate composition, and a catalyst present in sufficient amount to initiate an oligomerization reaction between a dihydroxy composition and the activated diaryl carbonate to form polycarbonate oligomers. The method further includes the steps of introducing a melted dihydroxy composition to the reaction mixture contained within the equilibration system, maintaining the reaction mixture contained within the vessel at an oligomerization temperature, said oligomerization temperature being below the melting point the dihydroxy composition, and sufficiently high to allow formation of a homogeneous melt within the vessel, and continuously drawing off a product stream from the equilibration system, wherein the product stream comprises a polycarbonate oligomer mixture. This polycarbonate oligomer mixture is suitably used as a feed stock for producing polycarbonate in a polycondensation system. The polycarbonate is suitably used for the preparation of molded articles.
    • 本发明提供一种制备聚碳酸酯低聚物,聚碳酸酯,由聚碳酸酯形成的模制品的方法和用于制备聚碳酸酯的装置。 首先通过以下步骤制备低聚物混合物,所述步骤包括提供包含容器,容器内的反应混合物的平衡系统和用于混合包含在容器内的反应混合物的装置,其中反应混合物包含熔融的活化碳酸二芳基酯组合物和 存在足够量的催化剂以引发二羟基组合物和活化的碳酸二芳基酯之间的低聚反应以形成聚碳酸酯低聚物。 该方法还包括以下步骤:将熔融的二羟基组合物引入平衡系统中包含的反应混合物中,将容器内的反应混合物保持在低聚温度,所述低聚温度低于二羟基组合物的熔点,并且足够高 以允许在容器内形成均匀的熔体,并且从平衡系统连续地抽出产物流,其中产物流包含聚碳酸酯低聚物混合物。 该聚碳酸酯低聚物混合物适合用作在缩聚体系中制造聚碳酸酯的原料。 聚碳酸酯适合用于制备模塑制品。
    • 8. 发明授权
    • Preparation of polycarbonate having a predetermined molecular weight and level of endcapping
    • 具有预定分子量和封端水平的聚碳酸酯的制备
    • US06399739B1
    • 2002-06-04
    • US09934929
    • 2001-08-22
    • Patrick Joseph McCloskeyAlberto NisoliWarren William Reilly
    • Patrick Joseph McCloskeyAlberto NisoliWarren William Reilly
    • C08G6400
    • C08G64/307
    • A melt method of preparing polycarbonate having a predetermined number average molecular weight and percent endcapping is described. A computerized process model is used to determine the reaction parameters to be employed in order to furnish the product polycarbonate possessing the desired Mn and %EC. Reaction parameters of importance include a suitable starting molar ratio of diaryl carbonate to dihydroxy aromatic compound, the most appropriate reaction time, reaction temperature and pressure ranges. The target polycarbonate is then prepared using reaction parameters indicated by the process model in a reactor which forms an element of the process model. Characteristics of the reactor which may be included in the process model include agitation rate and reflux ratio during the distillative removal of hydroxy aromatic compound formed as a by-product during the polymerization.
    • 描述了制备具有预定数均分子量和百分比封端的聚碳酸酯的熔融方法。 使用计算机化过程模型来确定要使用的反应参数,以便提供具有期望的Mn和%EC的产物聚碳酸酯。 重要的反应参数包括碳酸二芳基酯与二羟基芳族化合物的合适起始摩尔比,最合适的反应时间,反应温度和压力范围。 然后使用形成过程模型元素的反应器中由过程模型指示的反应参数制备目标聚碳酸酯。 可以包括在过程模型中的反应器的特征包括在蒸馏除去在聚合期间作为副产物形成的羟基芳族化合物的搅拌速率和回流比。
    • 10. 发明授权
    • Method for making polycarbonate
    • 制作聚碳酸酯的方法
    • US06569985B2
    • 2003-05-27
    • US09924137
    • 2001-08-08
    • Patrick Joseph McCloskeyAlberto NisoliWarren William Reilly
    • Patrick Joseph McCloskeyAlberto NisoliWarren William Reilly
    • C08G6400
    • C08G64/307
    • Polycarbonates having a high level of endcapping and containing a low level of Fries rearrangement product are prepared from dihydroxy aromatic compounds, such as bisphenol A, and diaryl carbonates such as diphenyl carbonate in a two stage process involving a tetraalkyl phosphonium carboxylate catalyzed oligomerization of the reactants in a first reaction stage followed by the addition of an alkali metal hydroxide co-catalyst in the second stage of the polymerization reaction. The late addition of the co-catalyst provides improved polymerization reaction rates as judged by higher polycarbonate molecular weights. The amount of alkali metal hydroxide co-catalyst is small thus avoiding the formation of excessive amounts of Fries product. The method has been used to provide Fries product levels between 200 and 800 parts per million in polycarbonates having Mn values between 7,500 and 8,500 Daltons.
    • 具有高水平的封端并含有低含量的Fries重排产物的聚碳酸酯由二羟基芳族化合物如双酚A和碳酸二芳基酯如碳酸二苯酯在涉及四烷基鏻羧酸酯催化的反应物低聚的两步法中制备 在第一反应阶段,然后在聚合反应的第二阶段加入碱金属氢氧化物助催化剂。 通过较高的聚碳酸酯分子量判断,辅助催化剂的晚期添加提供了改进的聚合反应速率。 碱金属氢氧化物助催化剂的量很小,从而避免形成过量的油炸产品。 该方法已经被用于在Mn值在7,500和8,500道尔顿之间的聚碳酸酯中提供200至800ppm之间的Fries产品水平。