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    • 35. 发明授权
    • Method of polycarbonate preparation by solid state polymerization
    • 通过固态聚合制备聚碳酸酯的方法
    • US06518391B1
    • 2003-02-11
    • US09911505
    • 2001-07-24
    • Patrick Joseph McCloskeyJames DayPaul Michael Smigelski, Jr.Timothy Brydon Burnell
    • Patrick Joseph McCloskeyJames DayPaul Michael Smigelski, Jr.Timothy Brydon Burnell
    • C08G6400
    • C08G64/307C08G64/06
    • Solid state polymerization of partially crystalline polycarbonate oligomers bearing ester-substituted terminal groups occurs at useful reaction rates despite their high level of endcapping. Partially crystalline polycarbonate oligomers having ester substituted terminal groups may be obtained in a single step by reaction of an ester substituted diaryl carbonate such as bis-methyl salicyl carbonate with a dihydroxy aromatic compound such as bisphenol A in the presence of a transesterification catalyst such as sodium hydroxide. Alternatively, amorphous oligomeric polycarbonates incorporating ester substituted endgroups may be obtained through careful control of the melt reaction conditions. The amorphous oligomeric polycarbonates are crystallized upon exposure to solvent vapor and subsequently undergo solid state polymerization at synthetically useful reaction rates.
    • 带有酯取代的端基的部分结晶的聚碳酸酯低聚物的固态聚合以有效的反应速率发生,尽管它们具有高水平的封端。 具有酯取代的末端基的部分结晶的聚碳酸酯低聚物可以通过酯交换催化剂如钠的存在下,酯取代的碳酸二碳酸酯如碳酸双甲基酯与二羟基芳族化合物如双酚A的反应在一个步骤中获得 氢氧化物。 或者,可以通过仔细控制熔融反应条件来获得引入酯取代的端基的无定形低聚聚碳酸酯。 无定形低聚聚碳酸酯在暴露于溶剂蒸气下结晶,随后在合成有用的反应速率下进行固态聚合。
    • 36. 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。
    • 37. 发明授权
    • Method for conducting solid state polymerization of polycarbonates
    • 聚碳酸酯的固态聚合方法
    • US06248858B1
    • 2001-06-19
    • US09192350
    • 1998-11-16
    • James DayGodavarthi Satyana Varadarajan
    • James DayGodavarthi Satyana Varadarajan
    • C08G6400
    • C08G64/20C08G63/64C08G64/40
    • Polymerization of polycarbonates is performed by first enhancing the crystallinity of a precursor polycarbonate, such as an oligomer, by contact in pellet form with an alkanol in the liquid or vapor state as non-solvent, and then conducting solid state polymerization in a stream of inert gas such as nitrogen. The solid state polymerization operation includes a stage of heating at a constant temperature in the range of about 215-225° C., optionally combined with a first heating stage at a constant temperature in the range of about 180-190° C. The method is adaptable to continuous operation and produces a polycarbonate having a number average molecular weight, as determined by gel permeation chromatography relative to polystyrene, of at least 15,000.
    • 聚碳酸酯的聚合通过首先通过以颗粒形式与液体或蒸气状态的链烷醇作为非溶剂接触来提高前体聚碳酸酯如低聚物的结晶度,然后在惰性气流中进行固态聚合 气体如氮气。 固态聚合操作包括在约215-225℃的恒定温度下加热的阶段,任选地在约180-190℃的恒定温度下与第一加热阶段组合。方法 适用于连续操作,并且通过凝胶渗透色谱法相对于聚苯乙烯产生数均分子量为至少15,000的聚碳酸酯。
    • 39. 发明授权
    • Method of making permanent magnet rotors
    • 制造永磁转子的方法
    • US5288447A
    • 1994-02-22
    • US20968
    • 1993-02-22
    • James Day
    • James Day
    • B29C33/02B29C43/18B29C70/72
    • B29C43/18B29C70/72B29C33/02B29K2503/06B29K2995/0008Y10S264/58
    • A plastic binder is milled to a powder, preferably having a particle size equal to the mean size of flakes of permanent magnet material, and dry mixed with the magnetic flakes. A molding fixture is heated to a temperature higher than that of the melting point of the plastic binder. A rotor core, having a rounded upper edge for molding a thin cylindrical magnet thereon, of solid or laminated soft magnetic material is prepared and placed in the molding fixture and brought up to the molding temperature. The mixture is poured in measured amounts into the upper chamber of the hot molding fixture and then compressed and melted. The fluid mixture is transferred into a molding cavity surrounding the rotor core in the lower chamber and cooled. After cooling, the finished permanent magnet rotor is ejected. Advantageously, by this method, the proportion of magnetic material to plastic may be increased to approximately 80%/20% magnetic material to plastic by volume, and the magnets may be made thinner.
    • 将塑料粘合剂研磨成粉末,优选具有等于永磁材料薄片的平均尺寸的粒度,并与磁性薄片干混。 将成型夹具加热到比塑料粘合剂的熔点高的温度。 制备具有固体或层压软磁材料的用于模制其上的薄圆柱形磁体的圆形上边缘的转子芯,并将其放置在模制夹具中并达到模制温度。 将混合物以测量的量倒入热成型固定装置的上腔室中,然后压缩并熔化。 将流体混合物转移到围绕下室中的转子芯的模制腔中并冷却。 冷却后,完成永久磁铁转子的喷射。 有利地,通过这种方法,磁性材料与塑料的比例可以增加到塑料的大约80%/ 20%的磁性材料,并且可以使磁体变薄。