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    • 81. 发明授权
    • Non-cyclopentadienyl-based chromium catalysts for olefin polymerization
    • 用于烯烃聚合的非环戊二烯基铬催化剂
    • US09422375B2
    • 2016-08-23
    • US14931258
    • 2015-11-03
    • Dow Global Technologies LLC
    • Matthew D. ChristiansonTimothy S. De VriesRobert D J FroeseMatthias S. OberJasson T. PattonDuane R. RomerGordon R. RoofLixin SunEndre SzuromiCurt N. TheriaultDean M. WelshTimothy T. WenzelPaul H. Moran
    • C07F11/00C08F4/78C08F10/00C08F210/06C08F110/06C08F110/02
    • C08F4/78C07F11/00C08F10/00C08F110/02C08F110/06C08F210/06C08F4/69112C08F210/16C08F2500/15
    • Provided is a non-cyclopentadienyl-based chromium-ligand complex, preferably a chromium-ligand complex of formula (J): LCr(RA)m(D)k (J), wherein L is a non-Cp monoanionic ligand; Cr (chromium) is in a formal oxidation state of +3 or +2; when Cr formally is Cr+3, either m is 1 and RA is hydrocarbylene (a hydrocarbylene chromium-ligand complex of formula (J)) or m is 2 and each RA independently is hydrocarbyl (a dihydrocarbyl chromium-ligand complex of formula (J)), wherein each hydrocarbyl or hydrocarbylene of RA independently is unsubstituted or substituted by from 1 to 5 RAS; each RAS independently is a neutral aprotic heteroalkyl, neutral aprotic heterocycloalkyl, neutral aprotic heteroaryl, or neutral aprotic aryl; when Cr formally is Cr+2, m is 1 and RA is hydrocarbyl (a hydrocarbyl chromium-ligand complex of formula (J)); k is an integer of 0 or 1; D is absent when k is 0 or D is a neutral ligand when k is 1; wherein the chromium-ligand complex of formula (J) is overall neutral and lacks a cyclopentadienyl-based (Cp-based) moiety. Also provided is a chromium catalyst comprising or prepared from the complex. Also provided is a process of making the catalyst and a process employing the chromium catalyst for polymerizing the olefin monomer, especially a straight chain 1-alkene, to prepare the polyolefin, especially a partially chain-straightened poly(1-alkene) or olefin block copolymer. Further provided is the partially chain-straightened poly(1-alkene) or olefin block copolymer prepared thereby. Also provided is a high throughput workflow.
    • 提供非环戊二烯基铬配体络合物,优选式(J)的铬配体络合物:LCr(RA)m(D)k(J),其中L是非Cp单阴离子配体; Cr(铬)处于+3或+2的正式氧化态; 当Cr正式为Cr + 3时,m为1,RA为亚烃基(式(J))的亚烃基铬 - 配体配合物)或m为2,各RA独立地为烃基(式(J)的二烃基铬 - 配体络合物 )),其中RA的各个烃基或亚烃基独立地未被取代或被1至5个RAS取代; 每个RAS独立地是中性非质子杂烷基,中性非质子杂环烷基,中性非质子杂芳基或中性非质子性芳基; 当Cr正式为Cr + 2时,m为1,RA为烃基(式(J))的烃基铬 - 配体络合物); k是0或1的整数; 当k为0时,D不存在,或当k为1时D为中性配体; 其中式(J)的铬配体络合物是总体中性的,并且缺少基于环戊二烯基的(Cp-基)部分。 还提供了包含或由络合物制备的铬催化剂。 还提供了制备催化剂的方法和使用铬催化剂聚合烯烃单体,特别是直链1-烯烃的方法,以制备聚烯烃,特别是部分链改性的聚(1-烯烃)或烯烃嵌段 共聚物。 进一步提供由其制备的部分链直链化的聚(1-烯烃)或烯烃嵌段共聚物。 还提供了高吞吐量的工作流程。
    • 86. 发明授权
    • Process and apparatus for the polymerisation of olefins
    • 用于烯烃聚合的方法和设备
    • US09394382B2
    • 2016-07-19
    • US13988794
    • 2011-12-14
    • Andrew David BellJean-Louis ChamayouKevin Peter Ramsay
    • Andrew David BellJean-Louis ChamayouKevin Peter Ramsay
    • C08F2/34B01J8/24B01J8/44C08F10/00C08F110/02
    • C08F10/00C08F2/34C08F110/02C08F2/007
    • Process for gas phase polymerization of olefins in a fluidized bed reactor by (a) passing a fluidizing gas containing at least one olefin monomer through a fluidized bed of polymer particles in the presence of a polymerization catalyst to produce polymer at a polymer production rate of C Tonnes/hour, (b) withdrawing a first gaseous stream containing solid particles from the top of the reactor, (c) passing the first gaseous stream to a gas/solids separator, separating solid particles therefrom, and forming a second gaseous stream containing residual solid particles, (d) passing a portion of the second gaseous stream to at least one heat exchanger to remove heat of reaction whereby residual solid particles contact the heat exchanger, and (e) recycling a portion of the cooled stream from step (d) as the fluidizing gas in step (a). The heat exchangers have a heat exchange surface area which totals less than 120×C m2.
    • 在流化床反应器中通过(a)在聚合催化剂存在下使包含至少一种烯烃单体的流化气体通过聚合物颗粒的流化床将烯烃气相聚合的方法以聚合物生产速率C 吨/小时,(b)从反应器顶部排出含有固体颗粒的第一气态流,(c)将第一气流送至气体/固体分离器,从其中分离固体颗粒,并形成含有残留物的第二气流 固体颗粒,(d)将第二气流的一部分通入至少一个热交换器以除去反应热,由此残留的固体颗粒接触热交换器,和(e)将来自步骤(d)的冷却流的一部分再循环, 作为步骤(a)中的流化气体。 热交换器的热交换面积总计小于120×Cm2。