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公开(公告)号：US07473811B2
公开(公告)日：2009-01-06
申请号：US10986368
申请日：2004-11-12
申请人： Isto Eilos , Antti Pyhälahti , Matti Nurminen , Veli-Matti Purola
发明人： Isto Eilos , Antti Pyhälahti , Matti Nurminen , Veli-Matti Purola
IPC分类号： C07C5/03
CPC分类号： C10G65/04 , B01J8/0453 , B01J8/16 , B01J2208/00256 , C07C5/03 , C07C2521/04 , C07C2523/755 , C10G45/00 , C10G49/002 , C07C11/02
摘要： The present invention relates to a process for the hydrogenation of olefins. The process comprises hydrogenation of a feed stock comprising more than 90 wt-% of olefins, carried out in a hydrogenation reactor comprising at least two reaction stages, wherein the feed stock is hydrogenated in the first reaction stage equipped with a cooling circuit and comprising a first and an optional second catalyst bed, and the effluent from the first reaction stage is hydrogenated in the final reaction stage comprising one or more catalyst beds and optionally equipped with a cooling circuit, the process is operated in trickling or pulse flow mode in a three phase reactor with a fixed catalyst bed and at least one catalyst of same or different type is used in each stage, the catalyst having different particle size and/or optionally different shape in at least two stages.
摘要翻译： 本发明涉及烯烃氢化方法。 该方法包括在包括至少两个反应阶段的氢化反应器中进行的包含大于90重量％的烯烃的原料的氢化，其中原料在装备有冷却回路的第一反应阶段中被氢化并且包含 第一和任选的第二催化剂床，并且来自第一反应阶段的流出物在包括一个或多个催化剂床并且任选地具有冷却回路的最终反应阶段中被氢化，该过程以三滴流动或脉冲流动模式操作 在每个阶段使用具有固定催化剂床和至少一种相同或不同类型的催化剂的三相反应器，所述催化剂在至少两个阶段具有不同的粒度和/或任选不同的形状。
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公开(公告)号：US20050177014A1
公开(公告)日：2005-08-11
申请号：US10986368
申请日：2004-11-12
申请人： Isto Eilos , Antti Pyhalahti , Matti Nurminen , Veli-Matti Purola
发明人： Isto Eilos , Antti Pyhalahti , Matti Nurminen , Veli-Matti Purola
CPC分类号： C10G65/04 , B01J8/0453 , B01J8/16 , B01J2208/00256 , C07C5/03 , C07C2521/04 , C07C2523/755 , C10G45/00 , C10G49/002 , C07C11/02
摘要： The present invention relates to a process for the hydrogenation of olefins. The process comprises hydrogenation of a feed stock comprising more than 90 wt-% of olefins, carried out in a hydrogenation reactor comprising at least two reaction stages, wherein the feed stock is hydrogenated in the first reaction stage equipped with a cooling circuit and comprising a first and an optional second catalyst bed, and the effluent from the first reaction stage is hydrogenated in the final reaction stage comprising one or more catalyst beds and optionally equipped with a cooling circuit, the process is operated in trickling or pulse flow mode in a three phase reactor with a fixed catalyst bed and at least one catalyst of same or different type is used in each stage, the catalyst having different particle size and/or optionally different shape in at least two stages.
摘要翻译： 本发明涉及烯烃氢化方法。 该方法包括在包括至少两个反应阶段的氢化反应器中进行的包含大于90重量％的烯烃的原料的氢化，其中原料在装备有冷却回路的第一反应阶段中被氢化并且包含 第一和任选的第二催化剂床，并且来自第一反应阶段的流出物在包括一个或多个催化剂床并且任选地具有冷却回路的最终反应阶段中被氢化，该过程以三滴流动或脉冲流动模式操作 在每个阶段使用具有固定催化剂床和至少一种相同或不同类型的催化剂的三相反应器，所述催化剂在至少两个阶段具有不同的粒度和/或任选不同的形状。
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3.发明申请公开(公告)号：US20050053450A1
公开(公告)日：2005-03-10
申请号：US10929383
申请日：2004-08-31
CPC分类号： B65G1/0421 , B65G1/0407 , B66F9/07
摘要： A method and a system utilizing the same, comprising two or more stacker cranes, of which each is intended to transfer at least one load independently, comprising a horizontally movable driving carriage and a lifting carriage arranged therein and intended for the manipulation and vertical transfer of said load. At least two stacker cranes are arranged to move, when necessary, to such a relative position in which it is possible to manipulate and transfer a load resting on the support of both lifting carriages simultaneously and to perform the movements of the driving carriages and the lifting carriages in a synchronized manner.
摘要翻译： 一种采用该装置的方法和系统，包括两个或更多个堆垛起重机，每个起重机各自旨在独立地传递至少一个负载，包括水平移动的驱动滑架和设置在其中的用于操纵和垂直传送的驱动滑架 说负载 至少有两个堆垛机起重机必要时移动到这样的相对位置，在该相对位置中，可以同时操纵和传递搁在两个提升车架的支撑件上的负载，并且执行驱动支架的运动和提升 车厢以同步的方式。
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公开(公告)号：US07196238B2
公开(公告)日：2007-03-27
申请号：US10383763
申请日：2003-03-10
申请人： Matti Nurminen , Antti Pyhälahti , Pirjo Siira , Marja Tiitta
发明人： Matti Nurminen , Antti Pyhälahti , Pirjo Siira , Marja Tiitta
IPC分类号： C07C2/02
CPC分类号： C07C2/12 , Y02P20/127 , Y02P20/582 , C07C11/02
摘要： The invention relates to a process for dimerizing lower, olefinic hydrocarbons. In particular, the present invention concerns a process for dimerizing C3–, C4 and C5-olefins with a medium pore zeolite under process conditions allowing selective dimerization According to the invention, fresh olefinic hydrocarbon feedstock is fed to a reaction system including at least one reaction zone and at least one separation zone. The olefinic hydrocarbon feedstock is contacted with an acid catalyst at conditions in which at least a part of the olefins dimerizes. The effluent from the reaction zone is conducted to the separation zone where dimerized reaction product is separated from said effluent.
摘要翻译： 本发明涉及二烯化低级烯烃的方法。 特别地，本发明涉及一种使用中孔沸石进行二聚C 3 - ，C 4 - 和C 5 - 烯烃的方法 允许选择性二聚的条件根据本发明，将新鲜的烯烃原料进料到包括至少一个反应区和至少一个分离区的反应体系中。 烯烃原料在至少一部分烯烃二聚的条件下与酸催化剂接触。 将来自反应区的流出物进入分离区，其中二聚反应产物与所述流出物分离。
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5.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.
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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.
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公开(公告)号：US07038101B2
公开(公告)日：2006-05-02
申请号：US10235321
申请日：2002-09-05
CPC分类号： C07C2/08 , B01J2219/00006 , C07C2/06
摘要： A method for operating a dimerization reactor that receives a hydrocarbon feed and produces an output stream comprising a light hydrocarbon component, a dimer and an alcohol component comprises: (a) separating the first output stream into a top stream containing the light hydrocarbon and a bottom stream containing the dimer, with the alcohol being present in the top stream or the bottom stream or both; (b) contacting at least one of the bottom and top streams with a water stream so as to extract at least a major portion of the alcohol therefrom, thereby forming an water/alcohol stream; (c) contacting the water/alcohol stream with a hydrocarbon stream so as to extract at least a major portion of the alcohol present in the water/alcohol stream into the hydrocarbon stream, thereby forming an alcohol-enriched hydrocarbon stream; and (d) feeding the alcohol-enriched hydrocarbon stream into the dimerization reactor.
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