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    • 2. 发明申请
    • PRODUCTION METHOD OF ALPHA-OLEFIN LOW POLYMER
    • ALPHA-OLEFIN低聚物的生产方法
    • US20090326297A1
    • 2009-12-31
    • US12520096
    • 2007-10-22
    • Hiroki EmotoKei Yoshizuru
    • Hiroki EmotoKei Yoshizuru
    • C07C2/08
    • B01J31/2208B01J31/143B01J2231/12B01J2231/20B01J2531/62C07C2/08C08F10/00Y02P20/52C08F4/69C08F4/22C08F2/06
    • The object of the present invention is to provide a production method of an α-olefin low polymer, wherein a low polymer of an α-olefin is obtained in high yield. The present invention relates to that when an inert gas is allowed to exist in a gas phase part of a reactor 10 in the proportion of from 0.010 to 50.00% by volume, and an α-olefin is subjected to low polymerization reaction in a solvent in the presence of a chromium series catalyst comprising a chromium compound (a), at lest one nitrogen-containing compound (b) selected from the group consisting of an amine, an amide and an imide, and an aluminum-containing compound (c), an unreacted α-olefin and the solvent separated from a reaction liquid are circulated into the reactor 10, and where the proportion of the inert gas in the gas phase exceeds 50.00% by volume, the inert gas is discharged outside the reaction system from a gas phase part of the reactor 10 and/or a circulation piping 21 of an unreacted α-olefin.
    • 本发明的目的是提供一种α-烯烃低聚物的制备方法,其中以高产率获得α-烯烃的低聚物。 本发明涉及当将惰性气体以0.010至50.00%(体积)的比例存在于反应器10的气相部分中,并且在溶剂中使α-烯烃进行低聚合反应时 存在包含铬化合物(a)的铬系催化剂,至少一种选自胺,酰胺和酰亚胺和含铝化合物(c)的含氮化合物(b) 将未反应的α-烯烃和从反应液分离的溶剂循环到反应器10中,并且气相中惰性气体的比例超过50.00体积%时,惰性气体从气体排出到反应体系外 反应器10的相部分和/或未反应的α-烯烃的循环管道21。
    • 5. 发明申请
    • PRODUCTION METHOD OF ETHYLENE LOW POLYMER
    • 乙烯低聚物的生产方法
    • US20100036185A1
    • 2010-02-11
    • US12519778
    • 2007-10-25
    • Kazuyuki YokoyamaHiroki Emoto
    • Kazuyuki YokoyamaHiroki Emoto
    • C07C2/08
    • C07C2/32B01D1/225B01D3/143B01D3/148C07C7/04C07C2531/14C07C2531/22C08F10/00C08F110/02C08F210/16Y02P20/52C07C11/107C07C11/02C08F4/69C08F2500/02C08F210/14
    • The object of the present invention is to provide a method of recovering decene under the condition that a decomposition product of a chromium series catalyst and the like is difficult to form from a high boiler from which an ethylene low polymer has been separated, in a production method of an ethylene low polymer using a chromium series catalyst. The present invention relates to that an ethylene low polymer and a high boiler containing a chromium series catalyst, decene, tetradecene and a by-produced polymer are separated by evaporation operation from a reaction liquid containing an ethylene low polymer obtained by low polymerization reaction using a chromium series catalyst, and the high boiler is concentrated such that the tetradecene concentration is 5% by weight or more by an evaporative separator 70 and a liquid storage tank 80, and additionally, decene is evaporated and separated so as to satisfy the following general expression (1) wherein T is temperature (° C.) of a residual solution, and θ is residence time (min.) of a residual solution. [Exp. 1] θ/1.2EXP(850/T)≦1  (1)
    • 本发明的目的是提供一种回收癸烯的方法,该方法是在生产乙烯低聚合物的高锅炉难以形成铬系催化剂等的分解产物的条件下 使用铬系催化剂的乙烯低聚物的方法。 本发明涉及通过蒸发操作将乙烯低聚物和含有铬系催化剂,癸烯,十四碳烯和副产物聚合物的高锅炉从包含通过低聚合反应获得的乙烯低聚物的反应液体分离,使用 铬系催化剂,并且通过蒸发分离器70和液体储罐80将高沸点物浓缩至十四碳烯浓度为5重量%以上,此外,将癸烯蒸发分离,以满足以下通式 (1)其中T是残留溶液的温度(℃),θ是残留溶液的停留时间(min)。 [Exp。 1] theta / 1.2EXP(850 / T)