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1.发明申请Process for the running of a reactor suitable for heterogeneous reactions combined with reactions taking place in three-phase systems 有权用于运行适用于异相反应的反应与在三相系统中发生的反应相结合的方法公开(公告)号：US20070135527A1
公开(公告)日：2007-06-14
申请号：US10572516
申请日：2004-09-17
IPC分类号： C07C27/06
摘要： Process for the running of a reactor in which reactions take place in multiphase systems, wherein a gaseous phase prevalently consisting of CO and H2 is bubbled into a suspension of a solid in the form of particles (catalyst) in a liquid (prevalently reaction product), according to the Fischer-Tropsch technology.
摘要翻译： 其中反应发生在多相体系中的反应器运行的方法，其中将主要由CO和H 2 2组成的气相鼓泡成颗粒（催化剂）形式的固体的悬浮液， 在液体（主要是反应产物）中，根据费 - 托技术。
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公开(公告)号：US5827902A
公开(公告)日：1998-10-27
申请号：US907010
申请日：1997-08-06
申请人： Cristina Maretto , Vincenzo Piccolo
发明人： Cristina Maretto , Vincenzo Piccolo
CPC分类号： C10G2/342
摘要： Process for the optimum operation of a slurry bubble column reactor in the presence of a gas phase and a liquid phase, particularly for the Fischer-Tropsch reaction, characterized in that: 1) the process is carried out in a number of stages in series of .gtoreq.2;2) the flow conditions of the gas phase and liquid phase containing the solids are essentially plug flow conditions, with a gas rate of between 3 cm/s and 200 cm/s and a liquid rate of between 0 and 10 cm/s; 3) the concentration of solids in each stage is essentially constant and equal for each single stage, and is between 5 and 50% (vol./vol.).
摘要翻译： 在气相和液相存在下，特别是费 - 托反应的浆液鼓泡塔反应器的最佳操作的方法，其特征在于：1）该方法以多个阶段进行 > / = 2; 2）包含固体的气相和液相的流动条件基本上是气流条件，气体速率在3cm / s至200cm / s之间，液体速率在0至10cm / s之间; 3）每个阶段中固体的浓度基本上是恒定的，对于每个单一阶段是相同的，并且在5至50％（体积/体积）之间。
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3.发明授权Process for the running of a reactor suitable for heterogeneous reactions combined with reactions taking place in three-phase system 有权适用于异相反应的反应器的运行过程与在三相系统中发生的反应相结合公开(公告)号：US07820727B2
公开(公告)日：2010-10-26
申请号：US12370682
申请日：2009-02-13
IPC分类号： C07C27/00
摘要： Process for the running of a reactor in which reactions take place in multiphase systems, wherein a gaseous phase prevalently consisting of CO and H2 is bubbled into a suspension of a solid in the form of particles (catalyst) in a liquid (prevalently reaction product), according to the Fischer-Tropsch technology.
摘要翻译： 其中在多相体系中发生反应的反应器运行的方法，其中将主要由CO和H 2组成的气相鼓泡在液体（主要是反应产物）中的颗粒（催化剂）形式的固体的悬浮液中， ，根据费托技术。
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公开(公告)号：US06700030B2
公开(公告)日：2004-03-02
申请号：US10239400
申请日：2002-09-26
IPC分类号： C07C100
CPC分类号： B01J8/22 , B01J2208/0069 , B01J2208/00725 , Y10S585/925
摘要： A process for converting hydrocarbons in the presence of a catalyst is described that is carried out in a three-phase reactor in which the liquid Peclet number is in the range 0 (excluded) to about 10, with a superficial gas velocity Ug that is preferably less than 35 cm.s−1, to encourage gas transfer into the liquid phase and avoid too much attrition of the catalyst grains.
摘要翻译： 描述了在催化剂存在下转化烃的方法，其中在三相反应器中进行，其中液体派百列数在0（不包括）至约10的范围内，表观气体速度Ug优选为 小于35cm -1，以鼓励气体转移到液相中，并避免催化剂颗粒过度磨损。
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5.发明授权Process for regenerating a catalyst contained within a bubble-column reactor with draft-tube and process for the production of a hydrocarbon 有权用起泡管再生含有气泡塔式反应器内的催化剂的方法和用于生产烃的方法
公开(公告)号：US6162754A
公开(公告)日：2000-12-19
申请号：US147736
申请日：1999-03-18
IPC分类号： B01J38/10 , B01J8/22 , B01J38/48 , B01J38/58 , C07C1/04 , C07C9/02 , C10G2/00 , B01J20/34 , B01J38/56
CPC分类号： C10G2/342 , B01J8/226 , B01J38/48 , B01J2208/00132 , B01J2208/0084 , B01J2219/00033 , C07C1/049 , Y02P20/584
摘要： Continuous process for the production of prevalently heavy hydrocarbons starting from synthesis gas in the presence of a gas phase, a liquid and a solid catalyst, the above process being carried out using a bubble column, characterized in that the bubble column internally has: (a) at least one draft-tube; (b) at least one device for the inlet of the synthesis gas; (c) at least one device for the inlet of the regenerating gas; (d) at least one device for activating/interrupting the stream of regenerating gas; (e) optional devices suitable for minimizing the mixing of the synthesis gas with the regenerating gas.
摘要翻译： PCT No.PCT / EP98 / 03874 371 1999年3月18日 102（e）1999年3月18日PCT提交1998年6月20日PCT公布。 公开号WO99 / 00191 日期1999年1月7日在气相，液体和固体催化剂存在下从合成气开始生产普遍重质烃的连续方法，上述方法使用气泡塔进行，其特征在于气泡塔 内部具有：（a）至少一个通气管; （b）用于合成气入口的至少一个装置; （c）用于再生气体入口的至少一个装置; （d）用于激活/中断再生气体流的至少一个装置; （e）适于最小化合成气与再生气体的混合的可选装置。
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6.发明申请Process for the charging of a catalyst into a reactor suitable for reactions in heterogenous phase 有权将催化剂装入适用于异相的反应的反应器的方法公开(公告)号：US20070066690A1
公开(公告)日：2007-03-22
申请号：US10571125
申请日：2004-09-17
IPC分类号： C07C27/26
CPC分类号： C10G2/33 , B01J8/0015 , B01J8/22 , B01J2208/00752 , B01J2208/00787 , C10G2/342 , C10G2300/70
摘要： Process for the charging of a catalyst and for the running of a reactor in which reactions take place in multiphase systems, wherein a gaseous phase prevalently consisting of CO and H2 is bubbled into a suspension of a solid in the form of particles (catalyst) in a liquid (prevalently reaction product), according to the Fischer-Tropsch technology.
摘要翻译： 催化剂的装载和反应在多相体系中发生的反应器运行的方法，其中将主要由CO和H 2组成的气相鼓泡到颗粒（催化剂）形式的固体的悬浮液中 根据费 - 托技术的液体（主要是反应产物）。
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7.发明授权公开(公告)号：US07579382B2
公开(公告)日：2009-08-25
申请号：US10571125
申请日：2004-09-17
IPC分类号： C07C27/00
CPC分类号： C10G2/33 , B01J8/0015 , B01J8/22 , B01J2208/00752 , B01J2208/00787 , C10G2/342 , C10G2300/70
摘要： Process for the charging of a catalyst and for the running of a reactor in which reactions take place in multiphase systems, wherein a gaseous phase prevalently consisting of CO and H2 is bubbled into a suspension of a solid in the form of particles (catalyst) in a liquid (prevalently reaction product), according to the Fischer-Tropsch technology.
摘要翻译： 催化剂的装载和反应在多相体系中发生的反应器运行的方法，其中将主要由CO和H 2组成的气相鼓泡到颗粒（催化剂）形式的固体的悬浮液中 根据费 - 托技术的液体（主要是反应产物）。
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8.发明申请PROCESS FOR THE RUNNING OF A REACTOR SUITABLE FOR HETEROGENEOUS REACTIONS COMBINED WITH REACTIONS TAKING PLACE IN THREE-PHASE SYSTEM 有权用于反应器运行的反应器的过程与用于在三相系统中的位置相结合的异构反应公开(公告)号：US20090197980A1
公开(公告)日：2009-08-06
申请号：US12370682
申请日：2009-02-13
IPC分类号： C07C27/00
摘要： Process for the running of a reactor in which reactions take place in multiphase systems, wherein a gaseous phase prevalently consisting of CO and H2 is bubbled into a suspension of a solid in the form of particles (catalyst) in a liquid (prevalently reaction product), according to the Fischer-Tropsch technology.
摘要翻译： 其中在多相体系中发生反应的反应器运行的方法，其中将主要由CO和H 2组成的气相鼓泡在液体（主要是反应产物）中的颗粒（催化剂）形式的固体的悬浮液中， ，根据费托技术。
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9.发明授权Process for the running of a reactor suitable for heterogeneous reactions combined with reactions taking place in three-phase systems 有权用于运行适用于异相反应的反应与在三相系统中发生的反应相结合的方法公开(公告)号：US07550515B2
公开(公告)日：2009-06-23
申请号：US10572516
申请日：2004-09-17
IPC分类号： C07C27/00
摘要： Process for the running of a reactor in which reactions take place in multiphase systems, wherein a gaseous phase prevalently consisting of CO and H2 is bubbled into a suspension of a solid in the form of particles (catalyst) in a liquid (prevalently reaction product), according to the Fischer-Tropsch technology.
摘要翻译： 其中在多相体系中发生反应的反应器运行的方法，其中将主要由CO和H 2组成的气相鼓泡在液体（主要是反应产物）中的颗粒（催化剂）形式的固体的悬浮液中， ，根据费托技术。
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公开(公告)号：US06825237B2
公开(公告)日：2004-11-30
申请号：US10239395
申请日：2002-09-26
IPC分类号： C07C2700
CPC分类号： C10G2/342
摘要： A process for synthesising hydrocarbons by reacting a mixture comprising at least carbon monoxide and hydrogen in the presence of a catalyst is carried out in a three-phase reactor in which the liquid Peclet number is in the range 0 (excluded) to about 10, with a superficial gas velocity Ug that is preferably less than 35 cm.s−1, to encourage gas transfer into the liquid phase and avoid too much attrition of the catalyst grains.
摘要翻译： 在催化剂存在下通过使包含至少一氧化碳和氢气的混合物反应合成烃的方法是在三相反应器中进行的，其中液体派佩克数在0（不包括）至约10的范围内，与 表面气体速度Ug优选小于35cm -1，以促进气体转移到液相中并避免催化剂颗粒的过多磨损。
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