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    • 6. 发明授权
    • Hydrogen response Ziegler-Natta catalyst for narrowing MWD of polyolefin, method of making, method of using, and polyolefins made therewith
    • 用于使聚烯烃的MWD变窄的齐格勒 - 纳塔催化剂,制造方法,使用方法和由此制成的聚烯烃
    • US06486274B1
    • 2002-11-26
    • US09687688
    • 2000-10-13
    • Steven D. GrayTim J. Coffy
    • Steven D. GrayTim J. Coffy
    • C08F4614
    • C08F10/00C08F4/6567C08F4/6557
    • A Ziegler-Natta type catalyst having an improved hydrogen response provides for narrowing of the MWD of resulting polyolefins polymerized using such catalyst, with such catalyst generally made by a) contacting a soluble magnesium dialkoxide compound of the general formula Mg(OR″)2 with a halogenating agent capable of exchanging one halogen for one alkoxide to form a reaction product A, where R″ is a hydrocarbyl or substituted hydrocarbyl having from 1 to 20 carbon atoms; b) contacting reaction product A with a first halogenating/titanating agent to form reaction product B; and c) contacting reaction product B with a second halogenating/titanating agent to form a catalyst component; wherein in at least one of steps b) and c), the halogenating/titanating agent is a blend of Ti(OPr)4 and TiCl4. Catalyst components, catalysts, catalyst systems, polyolefin polymers, and methods of forming each are disclosed.
    • 具有改善的氢气响应的齐格勒 - 纳塔型催化剂使得使用这种催化剂聚合的所得聚烯烃的MWD变窄,通常用以下方法制备的催化剂:a)使通式Mg(OR“)2的可溶性二烷氧基镁化合物 与一种能够与一个卤素交换一个醇盐形成反应产物A的卤化剂,其中R“是具有1至20个碳原子的烃基或取代的烃基; b)使反应产物A与第一卤化/钛化剂接触以形成反应产物B; 和c)使反应产物B与第二卤化/钛化剂接触以形成催化剂组分; 其中在步骤b)和c)中的至少一个中,卤化/钛化剂是Ti(OPr)4和TiCl 4的共混物。 公开了催化剂组分,催化剂,催化剂体系,聚烯烃聚合物和各种形成方法。
    • 7. 发明申请
    • Process for Controlling Morphology of Ziegler-Natta Catalysts
    • 控制齐格勒 - 纳塔催化剂形态的方法
    • US20090023875A1
    • 2009-01-22
    • US11778262
    • 2007-07-16
    • Kayo VizziniHenry EnriquezSteven D. GrayTim J. CoffyDavid W. Knoeppel
    • Kayo VizziniHenry EnriquezSteven D. GrayTim J. CoffyDavid W. Knoeppel
    • B01J37/03C08F4/12
    • C08F10/00C08F210/16Y10T428/1345Y10T428/139C08F4/6546C08F4/6541
    • Disclosed is a process for making a Ziegler-Natta catalyst having controlled particle size and distribution. It comprises altering the precipitation of a catalyst component from a catalyst synthesis solution including a soluble magnesium containing catalyst precursor by controlling the concentration of either the soluble magnesium containing catalyst precursor, wherein the average particle size of the catalyst component is increased, and the particle size distribution increased, with a decreased concentration of the soluble magnesium containing catalyst precursor; or of the precipitating agent, wherein the average particle size of the catalyst component is increased, and the particle size distribution increased with an increased concentration of the precipitating agent. Use of the invention enables improved catalyst consistency regardless of production scale and customizing of catalyst morphology to desired polymer morphology. The novel catalyst components may be used to prepare polymers, and end-use articles therefrom, having desirable properties. It is emphasized that this abstract is provided to comply with the rules requiring an abstract which will allow a searcher or other reader to quickly ascertain the subject matter of the technical disclosure. It is submitted with the understanding that it will not be used to interpret or limit the scope or meaning of the claims.
    • 公开了一种制备具有受控粒度和分布的齐格勒 - 纳塔催化剂的方法。 其包括通过控制可溶性含镁催化剂前体的浓度来改变催化剂组分从包括可溶性镁的催化剂前体的催化剂合成溶液中的沉淀,其中催化剂组分的平均粒径增加,并且颗粒尺寸 分布增加,可溶性含镁催化剂前体的浓度降低; 或沉淀剂,其中催化剂组分的平均粒度增加,并且随着沉淀剂浓度的增加,粒度分布增加。 使用本发明能够改善催化剂的一致性,而不管生产规模如何,催化剂形态定制成所需的聚合物形态。 新颖的催化剂组分可用于制备聚合物及其最终用途制品,具有期望的性能。 要强调的是,该摘要被提供以符合要求摘要的规则,这将允许搜索者或其他读者快速确定技术公开的主题。 提交它的理解是,它不会用于解释或限制权利要求的范围或含义。
    • 9. 发明授权
    • Process for controlling morphology of Ziegler-Natta catalysts
    • 控制齐格勒 - 纳塔催化剂形态的方法
    • US08063159B2
    • 2011-11-22
    • US11778262
    • 2007-07-16
    • Kayo VizziniHenry EnriquezSteven D. GrayTim J. CoffyDavid W. Knoeppel
    • Kayo VizziniHenry EnriquezSteven D. GrayTim J. CoffyDavid W. Knoeppel
    • C08F4/00
    • C08F10/00C08F210/16Y10T428/1345Y10T428/139C08F4/6546C08F4/6541
    • Disclosed is a process for making a Ziegler-Natta catalyst having controlled particle size and distribution. It comprises altering the precipitation of a catalyst component from a catalyst synthesis solution including a soluble magnesium containing catalyst precursor by controlling the concentration of either the soluble magnesium containing catalyst precursor, wherein the average particle size of the catalyst component is increased, and the particle size distribution increased, with a decreased concentration of the soluble magnesium containing catalyst precursor; or of the precipitating agent, wherein the average particle size of the catalyst component is increased, and the particle size distribution increased with an increased concentration of the precipitating agent. Use of the invention enables improved catalyst consistency regardless of production scale and customizing of catalyst morphology to desired polymer morphology. The novel catalyst components may be used to prepare polymers, and end-use articles therefrom, having desirable properties.
    • 公开了一种制备具有受控粒度和分布的齐格勒 - 纳塔催化剂的方法。 其包括通过控制可溶性含镁催化剂前体的浓度来改变催化剂组分从包括可溶性镁的催化剂前体的催化剂合成溶液中的沉淀,其中催化剂组分的平均粒径增加,并且颗粒尺寸 分布增加,可溶性含镁催化剂前体的浓度降低; 或沉淀剂,其中催化剂组分的平均粒度增加,并且随着沉淀剂浓度的增加,粒度分布增加。 使用本发明能够改善催化剂的一致性,而不管生产规模如何,催化剂形态定制成所需的聚合物形态。 新颖的催化剂组分可用于制备聚合物及其最终用途制品,具有期望的性能。
    • 10. 发明申请
    • Process for the production of polyethylene resin
    • 聚乙烯树脂生产工艺
    • US20090182100A1
    • 2009-07-16
    • US12008740
    • 2008-01-14
    • Gerhard K. GuentherSteven D. GrayTim J. Coffy
    • Gerhard K. GuentherSteven D. GrayTim J. Coffy
    • C08F2/01
    • C08F210/16C08F110/02C08F2/001C08F2/00C08F2500/02C08F210/14C08F2500/01
    • Process for the polymerization of ethylene to produce a polymer of enhanced long chain branching. Ethylene and hydrogen are introduced into a first reaction zone to produce an ethylene polymer having a first molecular weight distribution. The polymer from the first reaction zone is applied to a second reaction zone along with ethylene and a C3-C8 alpha-olefin monomer. The second reaction zone is operated to produce a copolymer having a second molecular weight distribution different from the first molecular weight distribution. A polymer fluff of bimodal molecular weight distribution is recovered from the second reaction zone and heated to melt the fluff and then extruded. Concomitantly with the heating and or extrusion, the polymer fluff is treated in order to enhance the long chain branching and reduce the melt index MI5 of the polymer product.
    • 乙烯聚合制备增强长链支化聚合物的方法。 将乙烯和氢气引入第一反应区以产生具有第一分子量分布的乙烯聚合物。 来自第一反应区的聚合物与乙烯和C 3 -C 8α-烯烃单体一起施加到第二反应区。 操作第二反应区以产生具有不同于第一分子量分布的第二分子量分布的共聚物。 从第二反应区回收双峰分子量分布的聚合物绒毛,并加热熔化绒毛然后挤出。 伴随着加热和/或挤出,处理聚合物绒毛以增强长链支化并降低聚合物产物的熔体指数MI5。