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    • 22. 发明申请
    • Controlling particle size in HIPS using metal carboxylates
    • 使用金属羧酸盐控制HIPS中的粒径
    • US20050090614A1
    • 2005-04-28
    • US10691827
    • 2003-10-23
    • Cyril ChevillardJose Sosa
    • Cyril ChevillardJose Sosa
    • C08F279/02C08G63/48C08F4/00
    • C08F279/02C08F212/08
    • It has been discovered that certain compounds serve as particle size regulators when employed together with peroxide initiators for the polymerization of vinylaromatic monomers in the presence of diene polymers. Suitable compounds that can control particle size include, but are not necessarily limited to, cobalt naphthenate, zinc naphthenate, iron octoate, calcium octoate, zinc octoate, zinc neodecanoate, potassium octoate, copper naphthenate, calcium versalate, and the like. Use of these metal carboxylates when vinylaromatic monomers are polymerized in the presence of polybutadienes and peroxide initiators results in reduced polybutadiene particles. Grafting and morphology characteristics may also be improved.
    • 已经发现,当与二烯聚合物存在下乙烯基芳族单体聚合时,某些化合物与过氧化物引发剂一起使用时用作粒度调节剂。 可以控制颗粒尺寸的合适的化合物包括但不一定限于环烷酸钴,环烷酸锌,辛酸铁,辛酸钙,辛酸锌,新癸酸锌,辛酸钾,环烷酸铜,三钙酸钙等。 当乙烯基芳族单体在聚丁二烯和过氧化物引发剂存在下聚合时,这些金属羧酸盐的使用导致聚丁二烯颗粒减少。 接枝和形态特征也可以改善。
    • 23. 发明授权
    • Metallocene catalyzed propylene-&agr;-olefin random copolymer melt spun fibers
    • 茂金属催化的丙烯-α-烯烃无规共聚物熔纺纤维
    • US06476172B1
    • 2002-11-05
    • US09916476
    • 2001-07-27
    • Darek WachowiczCyril ChevillardLisa K. Albe
    • Darek WachowiczCyril ChevillardLisa K. Albe
    • C08F21006
    • D01F6/30C08F210/06C08F210/16Y10T428/2913C08F2500/20C08F2500/03
    • A fiber product drawn from an isotactic propylene copolymer of a C2, C4, C5, C6, C7 or C8 &agr;-olefin monomer produced in the presence of a metallocene catalyst characterized by a bridged chiral and stereorigid cyclopentadienyl or substituted cyclopentadienyl ligand structure of a transitional metal selected from group 4b, 5b, or 6b metals of the Periodic Table of Elements, the copolymer having a MFR less than 35, suitably about 30 or less. The copolymer is heated to a molten state and extruded to form a fiber preform. The preform is subjected to spinning at a spinning speed of at least 300 meters per minutes and subsequent drawing at a speed of up to about 1500 meters per minute to provide a draw ratio of at least 1.5 up to 5:1 to produce a continuous fiber having high tenacity of about 3.5 grams per denier and greater and good hand.
    • 在由金属茂催化剂存在下产生的C2,C4,C5,C6,C7或C8-α-烯烃单体的全同立构丙烯共聚物拉伸的纤维产物,其特征在于桥联的手性和立体刚性环戊二烯基或取代的环戊二烯基配体结构的过渡 选自元素周期表第4b,5b或6b族金属的金属,该共聚物的MFR小于35,合适地为约30或更小。 将共聚物加热至熔融状态并挤出以形成纤维预制件。 以每分钟至少300米的纺丝速度进行纺丝,随后以高达约1500米/分钟的速度拉伸,以提供至少1.5至5:1的拉伸比,以产生连续纤维 具有约3.5克/旦的高韧性和较好的手。
    • 26. 发明申请
    • Cocatalysts useful for preparing polyethylene pipe
    • 可用于制备聚乙烯管的助催化剂
    • US20070003720A1
    • 2007-01-04
    • US11471996
    • 2006-06-21
    • Steve GrayKayo VizziniCyril ChevillardVincent Barre
    • Steve GrayKayo VizziniCyril ChevillardVincent Barre
    • B32B27/08
    • C08F10/00C08F110/02Y10T428/1352C08F2500/12C08F2500/04C08F4/642
    • Commonly used triethyl aluminum and tri-isobutyl aluminum cocatalysts may be replaced in olefin polymerizations with a cocatalyst conforming to the formula AlRz(Xz)nLzm wherein Rz is a linear or branched organic moiety having at least 5 carbons and Xz is a linear or branched organic moiety having at least 5 carbons or heteroatom substituted organic moiety or a heterocyclic moiety having at least 4 atoms and may be anionic (n=2) or dianionic (n=1). Xz may also be hydrogen. The general formula is subject to the proviso that when n=2, each Xz may be the same or different and that both Xz moieties may not be hydrogen. The aluminum complex may also be in the form of an adduct complex where Lz is a Lewis base and m=1-3. Use of the invention enables production of a polyolefin pipe, such as polyethylene pipe, exhibiting improved processing, crack resistance and other desirable properties.
    • 通常使用的三乙基铝和三异丁基铝助催化剂可以用烯烃聚合反应替代,其中助催化剂符合式<?in-line-formula description =“In-line Formulas”end =“lead”?> AlR (X z) 其中R z是具有至少5个碳的直链或支链有机部分,X是直链或支链的有机部分 具有至少5个碳原子或杂原子取代的有机部分的部分或具有至少4个原子的杂环部分,并且可以是阴离子(n = 2)或二阴离子(n = 1)。 X 也可以是氢。 通式为条件,当n = 2时,每个X Z可以相同或不同,并且两个X z可以不是氢。 铝络合物也可以是加合物络合物的形式,其中L z是路易斯碱,m = 1-3。 使用本发明可以生产出聚烯烃管,如聚乙烯管,具有改善的加工性,抗裂性和其它所需的性能。
    • 29. 发明授权
    • Method for preparation of stable bitumen polymer compositions
    • 稳定沥青聚合物组合物的制备方法
    • US06441065B1
    • 2002-08-27
    • US09712672
    • 2000-11-14
    • Cyril ChevillardPaul BurasKevin P. KellyJames R. Butler
    • Cyril ChevillardPaul BurasKevin P. KellyJames R. Butler
    • C08L9500
    • C08L95/00C08L2666/04C08L53/00
    • The present invention provides a method for preparing an asphalt and thermoplastic elastomer composition. The process comprises preparing a crosslinking elastomer concentrate that is added to a heated asphalt cut in a stirred tank and then aged to improve SHRP high temperature grading. The crosslinking elastomer concentrate is prepared by adding thermoplastic elastomer and crosslinking agents to a suitable carrier oil, preferably an aromatic oil such as Hydrolene H series. This concentrate is maintained at a temperature that promotes association between the crosslinking agents and the elastomer for a time sufficient for association to substantially complete. In one embodiment, the associating time is in excess of 2 hours up to 24 hours. The asphalt is heated to a temperature sufficient to allow the stirring of the asphalt in the tank. The crosslinking thermoplastic elastomer concentrate is added to the asphalt while continuing to stir the asphalt. The mixture is stirred at a speed and for a period of time sufficient to increase the distribution of the elastomer into the asphalt. Stirring is continued for a period of time sufficient to improve the distribution of the crosslinking thermoplastic elastomer in the asphalt. The composition is then aged as a liquid for 12 to 48 hours to increase the SHRP high temperature grade.
    • 本发明提供一种制备沥青和热塑性弹性体组合物的方法。 该方法包括制备交联弹性体浓缩物,其加入到在搅拌槽中切割的加热沥青中,然后老化以改善SHRP高温分级。 交联弹性体浓缩物通过将热塑性弹性体和交联剂加入到合适的载体油,优选芳香油如氢化氢H系列中来制备。 该浓缩物保持在促进交联剂和弹性体之间缔合的温度足以与基本上完全结合的时间。 在一个实施方案中,缔合时间超过2小时至24小时。 将沥青加热到足以允许在罐中搅拌沥青的温度。 将交联热塑性弹性体浓缩物加入到沥青中,同时继续搅拌沥青。 将混合物以足以增加弹性体分配到沥青中的速度搅拌一段时间。 继续搅拌足以改善交联热塑性弹性体在沥青中的分布的时间。 然后将组合物作为液体陈化12至48小时以增加SHRP高温等级。