-
公开(公告)号：US08124820B2
公开(公告)日：2012-02-28
申请号：US11808879
申请日：2007-06-13
IPC分类号： C07C2/12
CPC分类号： C07C9/22 , B01D3/009 , C07C5/03 , C07C2529/06 , C07C2529/40 , C07C2529/70 , C10M105/04 , C10M107/10 , C10M2203/0206 , C10M2205/0285 , C10N2230/02 , C10N2230/08 , C10N2230/74 , C10N2260/02 , Y02P20/127
摘要： The present invention relates to a process for producing polyolefins wherein a feedstock comprising n-olefin or a mixture of n-olefins is dimerized in the presence of a solid acidic catalyst by passing the feedstock to a catalytic distillation apparatus comprising either a) a combination of a distillation column and a reactor comprising at least one catalyst bed, or b) a distillation column connected to one or more side reactors comprising at least one catalyst layer, recovering the unreacted n-olefin from the distillation column or the combination of the distillation column and the reactor at the upper part thereof as a side-stream to be combined with the feedstock, and the reaction product from the dimerization is hydrogenated.
摘要翻译： 本发明涉及一种生产聚烯烃的方法，其中包含正烯烃的原料或正烯烃的混合物在固体酸性催化剂的存在下被二聚化，通过将原料通过催化蒸馏装置，该催化蒸馏装置包括a） 蒸馏塔和包含至少一个催化剂床的反应器，或b）连接到一个或多个包含至少一个催化剂层的侧反应器的蒸馏塔，从蒸馏塔回收未反应的正烯烃或蒸馏塔的组合 和其上部的反应器作为与原料组合的侧流，并且来自二聚的反应产物被氢化。
-
公开(公告)号：US20070293712A1
公开(公告)日：2007-12-20
申请号：US11808879
申请日：2007-06-13
IPC分类号： C07C2/02
CPC分类号： C07C9/22 , B01D3/009 , C07C5/03 , C07C2529/06 , C07C2529/40 , C07C2529/70 , C10M105/04 , C10M107/10 , C10M2203/0206 , C10M2205/0285 , C10N2230/02 , C10N2230/08 , C10N2230/74 , C10N2260/02 , Y02P20/127
摘要： The present invention relates to a process for producing polyolefins wherein a feedstock comprising n-olefin or a mixture of n-olefins is dimerized in the presence of a solid acidic catalyst by passing the feedstock to a catalytic distillation apparatus comprising either a) a combination of a distillation column and a reactor comprising at least one catalyst bed, or b) a distillation column connected to one or more side reactors comprising at least one catalyst layer, recovering the unreacted n-olefin from the distillation column or the combination of the distillation column and the reactor at the upper part thereof as a side-stream to be combined with the feedstock, and the reaction product from the dimerization is hydrogenated.
摘要翻译： 本发明涉及一种生产聚烯烃的方法，其中包含正烯烃的原料或正烯烃的混合物在固体酸性催化剂的存在下被二聚化，通过将原料通过催化蒸馏装置，该催化蒸馏装置包括a） 蒸馏塔和包含至少一个催化剂床的反应器，或b）连接到一个或多个包含至少一个催化剂层的侧反应器的蒸馏塔，从蒸馏塔回收未反应的正烯烃或蒸馏塔的组合 和其上部的反应器作为与原料组合的侧流，并且来自二聚的反应产物被氢化。
-
公开(公告)号：US5767334A
公开(公告)日：1998-06-16
申请号：US602736
申请日：1996-04-08
申请人： Fredrik Nissfolk , Raimo Linnaila , Ivo Smeets , Vesa-Matti Lehtinen , Kauno Alastalo , Filip Thierie
发明人： Fredrik Nissfolk , Raimo Linnaila , Ivo Smeets , Vesa-Matti Lehtinen , Kauno Alastalo , Filip Thierie
IPC分类号： B01J27/32 , C07B61/00 , C07C2/14 , C07C2/20 , C07C7/04 , C07C9/22 , C07C11/02 , C08F4/06 , C08F4/14 , C08F6/06 , C08F6/08 , C08F10/00 , C07C2/08
CPC分类号： C07C11/02 , B01J27/32 , C07C2/20 , C07C7/04 , C07C2527/1213 , C07C2531/02 , C07C2531/04 , Y02P20/584
摘要： A method for removing catalyst from an olefinic oligomerization product includes the steps of oligomerizing one or more olefins in the presence of a BF.sub.3 cocatalyst complex, and distilling the oligomerization product while separating vaporized BF.sub.3 cocatalyst complex, the distillation step including, simultaneously to the separation of BF.sub.3 cocatalyst complex, a separation of vaporized unreacted monomer from a bottom product which becomes substantially free from BF.sub.3 cocatalyst complex.
摘要翻译： PCT No.PCT / BE95 / 00061 Sec。 371日期：1996年4月8日 102（e）日期1996年4月8日PCT归档1995年6月23日PCT公布。 公开号WO96 / 00201 日本1996年1月4日一种从烯烃低聚产物中除去催化剂的方法包括在BF 3助催化剂配合物存在下使一种或多种烯烃低聚的步骤，并在分离蒸发的BF 3助催化剂络合物的同时蒸馏低聚产物，蒸馏步骤包括， 同时分离BF 3助催化剂络合物，将蒸发的未反应单体与基本上不含BF 3助催化剂络合物的底部产物分离。
-
4.发明授权Method for recovering a gaseous boron trifluoride bf.sub.3 and the usage of the product formed in the method 失效用于回收气态三氟化硼bf3的方法和该方法中形成的产物的用途
公开(公告)号：US5254784A
公开(公告)日：1993-10-19
申请号：US811315
申请日：1991-12-20
CPC分类号： B01J27/32
摘要： The invention relates to a method for removing a boron trifluoride from the exhaust gases of a vacuum pump, which gases have been obtained when polymerizing .alpha.-olefines by using a BF.sub.3 -alcohol complex as a catalyst. In a vacuum distillation, the underpressure is achieved by means of a pump sealed with a fluid ring or by means of fluid jet with a torque or ejector pump, possibly assisted by a mechanical blaster, such as a propellant circulating pump. In this pump, the fluid ring or the fluid jet is formed by a cocatalyst forming a complex with the BF.sub.3 catalyst, which cocatalyst is an alcohol, preferably butanol.
-
公开(公告)号：US4956512A
公开(公告)日：1990-09-11
申请号：US271022
申请日：1988-11-14
申请人： Fredrik Nissfolk , Salme Koskimies , Peter Idelman , Matti Nurminen , Salla Roni
发明人： Fredrik Nissfolk , Salme Koskimies , Peter Idelman , Matti Nurminen , Salla Roni
IPC分类号： B01J31/40 , B01J38/00 , C07B61/00 , C07C1/00 , C07C2/32 , C07C67/00 , C10G50/02 , C10M107/02 , C10M107/10 , C10M177/00 , C10N70/00
CPC分类号： C10M177/00 , C10G50/02 , C10M107/02 , C10M2205/00 , C10M2205/02 , C10N2220/02
摘要： In producing lubricants by oligomerizing alpha-olefins with the aid of a catalyst of a BF.sub.3 and alcohol or carboxylic acid cocatalyst, the utilized catalyst complex can be recovered by distillation and reused as catalyst in a similar oligomerizing process.
-
-
-
-
搜索结果
5 条记录 (耗时 0.012 秒)
