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1. 发明申请

US20110301253A1 METHOD OF OPERATING A FLUID BED REACTOR 有权
标题翻译：流化床反应器的操作方法
公开(公告)号：US20110301253A1
公开(公告)日：2011-12-08
申请号：US13213640
申请日：2011-08-19
申请人： André Peter Steynberg , Berthold Berend Breman , Derk Willem Frederik Brilman
发明人： André Peter Steynberg , Berthold Berend Breman , Derk Willem Frederik Brilman
IPC分类号： C07C1/04 , B01J8/20 , B01J8/18
CPC分类号： B01J8/28 , B01J8/0055 , B01J8/065 , B01J8/067 , B01J8/1836 , B01J8/22 , B01J8/226 , B01J8/34 , B01J19/248 , B01J19/249 , B01J2208/00132 , B01J2208/0015 , B01J2208/0061 , B01J2208/0084 , B01J2208/022 , B01J2219/00015 , B01J2219/0002 , B01J2219/245 , B01J2219/2453 , B01J2219/2458 , B01J2219/2462 , B01J2219/247 , B01J2219/2474 , B01J2219/2481 , B01J2219/2496 , B01J2219/2497 , C10G2/344 , C10G2300/1022 , F28D7/00 , F28D7/163 , F28D9/00 , F28F9/22 , Y02P20/582
摘要： Method of operating a three-phase slurry reactor includes feeding at a low level at least one gaseous reactant into a vertically extending slurry body of solid particles suspended in a suspension liquid, the slurry body being contained in at least two vertically extending shafts housed within a common reactor shell, each shaft being divided into a plurality of vertically extending channels at least some of which are in slurry flow communication and the slurry body being present in at least some of the channels. The gaseous reactant is allowed to react as it passes upwardly through the slurry body present in at least some of the channels of the shafts, thereby to form a non-gaseous and/or a gaseous product. Gaseous product, if present, and/or unreacted gaseous reactant is allowed to disengage from the slurry body in a head space above the slurry body.
摘要翻译：操作三相浆料反应器的方法包括将低至少一种气态反应物进料到悬浮在悬浮液中的固体颗粒的垂直延伸的淤浆体中，所述淤浆体包含在容纳在悬浮液悬浮液中的至少两个垂直延伸的轴内共同的反应器壳体，每个轴被分成多个垂直延伸的通道，其中至少一些通道处于淤浆流动连通状态，并且淤浆体存在于至少一些通道中。当气态反应物向上通过存在于轴的至少一些通道中的淤浆体时，使其反应，从而形成非气态和/或气态产物。气体产物（如果存在）和/或未反应的气态反应物允许在浆料体上方的顶部空间中从浆料体脱离。

2. 发明授权

US07439274B2 Process for producing liquid, and, optionally, gaseous products from gaseous reactants 有权
标题翻译：用于从气态反应物生产液体和任选的气态产物的方法
公开(公告)号：US07439274B2
公开(公告)日：2008-10-21
申请号：US10555957
申请日：2004-05-12
申请人： André Peter Steynberg , Berthold Berend Breman
发明人： André Peter Steynberg , Berthold Berend Breman
IPC分类号： C07C27/00
CPC分类号： B01J8/1818 , B01J8/1827 , B01J8/1836 , B01J8/22 , B01J8/226 , B01J8/28 , B01J2208/00141 , B01J2208/00274 , B01J2208/00539 , B01J2208/0061 , C10G2/34 , C10G2/343 , C10G2300/4081 , Y02P20/582
摘要： A process (10) for producing liquid and, optionally, gaseous products from gaseous reactants includes feeding at a low level gaseous reactants (14) and, optionally, a portion of a recycle gas stream into a vertically extending slurry bed (70) of solid particles suspended in a suspension liquid inside a vessel (12), and feeding, as an additional gas feed (58), at least a portion of the recycle gas stream into the slurry bed (70) above the level at which the gaseous reactants (814) are fed into the slurry bed (70) and above the lower 20% of the vertical height of the slurry bed (70).
摘要翻译：用于从气体反应物生产液体和任选的气态产物的方法（10）包括将低级气态反应物（14）和任选的一部分循环气流进料到垂直延伸的固体淤浆床（70）中悬浮在容器（12）内的悬浮液体中的颗粒，以及作为另外的气体进料（58）将至少一部分循环气流进入浆液床（70）中的气态反应物 814）进料到浆料床（70）中并且高于浆料床（70）的垂直高度的20％以下。

3. 发明申请

US20110311402A1 METHOD OF OPERATING A THREE-PHASE SLURRY REACTOR 审中-公开
标题翻译：操作三相浆液反应器的方法
公开(公告)号：US20110311402A1
公开(公告)日：2011-12-22
申请号：US13216019
申请日：2011-08-23
申请人： André Peter Steynberg , Berthold Berend Breman , Derk Willem Frederik Brilman
发明人： André Peter Steynberg , Berthold Berend Breman , Derk Willem Frederik Brilman
IPC分类号： B01J8/18
CPC分类号： C10G2/342 , B01J8/1836 , B01J8/22 , B01J8/226 , B01J19/249 , B01J2208/0015 , B01J2208/022 , B01J2219/00015 , B01J2219/0002 , B01J2219/2453 , B01J2219/2458 , B01J2219/2462 , B01J2219/2474 , B01J2219/2481 , B01J2219/2496 , C10G2/32
摘要： A method of operating a three-phase slurry reactor includes feeding at a low level at least one gaseous reactant into a vertically extending slurry body of solid particles suspended in a suspension liquid, the slurry body being contained in a plurality of vertically extending horizontally spaced slurry channels inside a common reactor shell, the slurry channels being defined between vertically extending horizontally spaced divider walls or plates and each slurry channel having a height, width and breadth such that the height and breadth are much larger than the width. The gaseous reactant is allowed to react as it passes upwardly through the slurry body present in the slurry channels, thereby to form non-gaseous and/or gaseous product. Gaseous product and/or unreacted gaseous reactant is allowed to disengage from the slurry body in a head space above the slurry body.
摘要翻译：操作三相淤浆反应器的方法包括将低至少一种气态反应物进料到悬浮在悬浮液中的固体颗粒的垂直延伸的淤浆体中，浆料体包含在多个垂直延伸的水平间隔的浆料通道在共同的反应器壳体内，浆液通道限定在垂直延伸的水平隔开的分隔壁或板之间，并且每个浆料通道具有高度，宽度和宽度，使得高度和宽度远大于宽度。当气态反应物向上通过存在于浆料通道中的淤浆体时，使其反应，从而形成非气态和/或气态产物。允许气体产物和/或未反应的气态反应物在淤浆体上方的顶部空间中与浆料体脱离。

4. 发明申请

US20140107232A1 PROCESS FOR PRODUCING AT LEAST ONE PRODUCT FROM AT LEAST ONE GASEOUS REACTANT IN A SLURRY BED 有权
标题翻译：至少一种产品的方法，从一个浆料床中的至少一个气体反应器
公开(公告)号：US20140107232A1
公开(公告)日：2014-04-17
申请号：US14124107
申请日：2012-05-30
申请人： Berthold Berend Breman
发明人： Berthold Berend Breman
IPC分类号： C10G2/00
CPC分类号： C10G2/344 , B01J8/1827 , B01J8/1836 , B01J8/22 , B01J8/28 , B01J2208/00141 , B01J2208/00274 , C07C1/0455 , C10G2/32 , C10G2/332 , C10G2/342 , Y02P20/582
摘要： A process for producing at least one product from at least one gaseous reactant includes feeding the gaseous reactant, as a gaseous feed or as part of a gaseous feed which is ax an inlet superficial gas velocity of at least 0.5 m/s, into a vessel holding an expanded slurry bed of solid catalyst particles suspended in a suspension liquid so that the gaseous reactant can bubble upwardly through die slurry bed. The slurry bed has a catalyst loading of less than 14% by volume of degassed slurry. The gaseous reactant is allowed to react catalytically at a pressure above atmospheric pressure as the gaseous reactant bubbles upwardly through the slurry bed to produce at least one product. The product and any unreacted gaseous reactant are withdrawn from the vessel.
摘要翻译：用于从至少一种气态反应物生产至少一种产物的方法包括将气体反应物作为气体进料或作为至少0.5m / s的入口表观气体速度的气态进料的一部分进料到容器保持悬浮在悬浮液中的固体催化剂颗粒的膨胀淤浆床，使得气态反应物可以向上通过模浆料床。浆料床的催化剂负载量小于脱气浆料的14体积％。使气态反应物在高于大气压的压力下催化反应，因为气态反应物向上流过浆料床，以产生至少一种产物。将产物和任何未反应的气态反应物从容器中取出。

5. 发明授权

US09080108B2 Process for producing at least one product from at least one gaseous reactant in a slurry bed 有权
标题翻译：用于在淤浆床中从至少一种气态反应物生产至少一种产物的方法
公开(公告)号：US09080108B2
公开(公告)日：2015-07-14
申请号：US14124107
申请日：2012-05-30
申请人： Berthold Berend Breman
发明人： Berthold Berend Breman
IPC分类号： C07C27/06 , C10G2/00 , B01J8/18 , B01J8/22 , B01J8/28
CPC分类号： C10G2/344 , B01J8/1827 , B01J8/1836 , B01J8/22 , B01J8/28 , B01J2208/00141 , B01J2208/00274 , C07C1/0455 , C10G2/32 , C10G2/332 , C10G2/342 , Y02P20/582
摘要： A process for producing at least one product from at least one gaseous reactant includes feeding the gaseous reactant, as a gaseous feed or as part of a gaseous feed which is at an inlet superficial gas velocity of at least 0.5 m/s, into a vessel holding an expanded slurry bed of solid catalyst particles suspended in a suspension liquid so that the gaseous reactant can bubble upwardly through the slurry bed. The slurry bed has a catalyst loading of less than 14% by volume of degassed slurry. The gaseous reactant is allowed to react catalytically at a pressure above atmospheric pressure as the gaseous reactant bubbles upwardly through the slurry bed to produce at least one product. The product and any unreacted gaseous reactant are withdrawn from the vessel.
摘要翻译：用于从至少一种气态反应物生产至少一种产物的方法包括将气态反应物作为气态进料或作为入口表观气体速度为至少0.5m / s的气态进料的一部分进料到容器保持悬浮在悬浮液中的固体催化剂颗粒的膨胀淤浆床，使得气态反应物可以向上通过淤浆床。浆料床的催化剂负载量小于脱气浆料的14体积％。使气态反应物在高于大气压的压力下催化反应，因为气态反应物向上流过浆料床，以产生至少一种产物。将产物和任何未反应的气态反应物从容器中取出。

6. 发明申请

US20140128483A1 PROCESS FOR PRODUCING AT LEAST ONE PRODUCT FROM AT LEAST ONE GASEOUS REACTANT IN A SLURRY BED 有权
标题翻译：至少一种产品的方法，从一个浆料床中的至少一个气体反应器
公开(公告)号：US20140128483A1
公开(公告)日：2014-05-08
申请号：US14123994
申请日：2012-05-30
申请人： Berthold Berend Breman
发明人： Berthold Berend Breman
IPC分类号： C10G2/00
CPC分类号： C10G2/32 , B01J8/1827 , B01J8/1836 , B01J8/22 , B01J8/28 , B01J2208/00141 , B01J2208/00274 , C10G2/332 , C10G2/342 , Y02P20/582
摘要： A process for producing at least one product from at least one gaseous reactant includes feeding the gaseous reactant, as a gaseous feed or as part of a gaseous feed which is at an inlet superficial gas velocity of at least 0.5 m/s, into a vessel holding an expanded slurry bed of solid catalyst particles suspended in a suspension liquid so that the gaseous reactant can bubble upwardly through the slurry bed. The slurry bed has a catalyst loading of at least 20% by volume of degassed slurry. The gaseous reactant s allowed to react catalytically at a pressure above atmospheric pressure as the gaseous reactant bubbles upwardly through the slurry bed to produce at least one product. The product and any unreacted gaseous reactant are withdrawn from the vessel.
摘要翻译：用于从至少一种气态反应物生产至少一种产物的方法包括将气态反应物作为气态进料或作为入口表观气体速度为至少0.5m / s的气态进料的一部分进料到容器保持悬浮在悬浮液中的固体催化剂颗粒的膨胀淤浆床，使得气态反应物可以向上通过淤浆床。浆料床具有至少20体积％的脱气浆料的催化剂负载量。气态反应物在高于大气压的压力下催化反应，因为气态反应物向上通过浆料床向上产生至少一种产物。将产物和任何未反应的气态反应物从容器中取出。

7. 发明申请

US20080146683A1 Method of Operating a Fluid Bed Reactor 有权
标题翻译：操作流化床反应器的方法
公开(公告)号：US20080146683A1
公开(公告)日：2008-06-19
申请号：US11908923
申请日：2006-03-17
申请人： Andre Peter Steynberg , Berthold Berend Breman , Derk Willem Frederik Brilman
发明人： Andre Peter Steynberg , Berthold Berend Breman , Derk Willem Frederik Brilman
IPC分类号： C07C27/06 , B01J8/04
CPC分类号： B01J8/28 , B01J8/0055 , B01J8/065 , B01J8/067 , B01J8/1836 , B01J8/22 , B01J8/226 , B01J8/34 , B01J19/248 , B01J19/249 , B01J2208/00132 , B01J2208/0015 , B01J2208/0061 , B01J2208/0084 , B01J2208/022 , B01J2219/00015 , B01J2219/0002 , B01J2219/245 , B01J2219/2453 , B01J2219/2458 , B01J2219/2462 , B01J2219/247 , B01J2219/2474 , B01J2219/2481 , B01J2219/2496 , B01J2219/2497 , C10G2/344 , C10G2300/1022 , F28D7/00 , F28D7/163 , F28D9/00 , F28F9/22 , Y02P20/582
摘要： Method of operating a three-phase slurry reactor includes feeding at a low level at least one gaseous reactant into a vertically extending slurry body of solid particles suspended in a suspension liquid, the slurry body being contained in at least two vertically extending shafts housed within a common reactor shell, each shaft being divided into a plurality of vertically extending channels at least some of which are in slurry flow communication and the slurry body being present in at least some of the channels. The gaseous reactant is allowed to react as it passes upwardly through the slurry body present in at least some of the channels of the shafts, thereby to form a non-gaseous and/or a gaseous product. Gaseous product, if present, and/or unreacted gaseous reactant is allowed to disengage from the slurry body in a head space above the slurry body.
摘要翻译：操作三相浆料反应器的方法包括将低至少一种气态反应物进料到悬浮在悬浮液中的固体颗粒的垂直延伸的淤浆体中，所述淤浆体包含在容纳在悬浮液悬浮液中的至少两个垂直延伸的轴内共同的反应器壳体，每个轴被分成多个垂直延伸的通道，其中至少一些通道处于淤浆流动连通状态，并且淤浆体存在于至少一些通道中。当气态反应物向上通过存在于轴的至少一些通道中的淤浆体时，使其反应，从而形成非气态和/或气态产物。气体产物（如果存在）和/或未反应的气态反应物允许在浆料体上方的顶部空间中从浆料体脱离。

8. 发明申请

US20080114083A1 Method of Operating a Three-Phase Slurry Reactor 有权
标题翻译：操作三相浆料反应器的方法
公开(公告)号：US20080114083A1
公开(公告)日：2008-05-15
申请号：US11908916
申请日：2006-03-17
申请人： Andre Peter Steynberg , Berthold Berend Breman , Derk Willem Frederick Brilman
发明人： Andre Peter Steynberg , Berthold Berend Breman , Derk Willem Frederick Brilman
IPC分类号： C07C27/26 , B01J8/18
CPC分类号： C10G2/342 , B01J8/1836 , B01J8/22 , B01J8/226 , B01J19/249 , B01J2208/0015 , B01J2208/022 , B01J2219/00015 , B01J2219/0002 , B01J2219/2453 , B01J2219/2458 , B01J2219/2462 , B01J2219/2474 , B01J2219/2481 , B01J2219/2496 , C10G2/32
摘要： A method of operating a three-phase slurry reactor includes feeding at a low level at least one gaseous reactant into a vertically extending slurry body of solid particles suspended in a suspension liquid, the slurry body being contained in a plurality of vertically extending horizontally spaced slurry channels inside a common reactor shell, the slurry channels being defined between vertically extending horizontally spaced divider walls or plates and each slurry channel having a height, width and breadth such that the height and breadth are much larger than the width. The gaseous reactant is allowed to react as it passes upwardly through the slurry body present in the slurry channels, thereby to form non-gaseous and/or gaseous product. Gaseous product and/or unreacted gaseous reactant is allowed to disengage from the slurry body in a head space above the slurry body.
摘要翻译：操作三相淤浆反应器的方法包括将低至少一种气态反应物进料到悬浮在悬浮液中的固体颗粒的垂直延伸的淤浆体中，浆料体包含在多个垂直延伸的水平间隔的浆料通道在共同的反应器壳体内，浆液通道限定在垂直延伸的水平隔开的分隔壁或板之间，并且每个浆料通道具有高度，宽度和宽度，使得高度和宽度远大于宽度。当气态反应物向上通过存在于浆料通道中的淤浆体时，使其反应，从而形成非气态和/或气态产物。允许气体产物和/或未反应的气态反应物在淤浆体上方的顶部空间中与淤浆体脱离。

9. 发明授权

US06413429B1 Process and apparatus for liquid-liquid extraction 失效
标题翻译：液 - 液萃取工艺及装置
公开(公告)号：US06413429B1
公开(公告)日：2002-07-02
申请号：US09754159
申请日：2001-01-04
申请人： Berthold Berend Breman , Jan Visser
发明人： Berthold Berend Breman , Jan Visser
IPC分类号： B02D1100
CPC分类号： B01D11/0449 , B01D11/0457 , Y10S210/05
摘要： Claimed are a process and an apparatus for extracting a component dissolved in a liquid by means of liquid-liquid extraction using an extraction liquid which is immiscible or only partially miscible with the liquid, in which process the extraction liquid is dispersed in the liquid in a dispersion apparatus and then coalesced in a coalescer, after which the ex traction liquid, the specific weight of which differs by at least 5% from the specific weight of the liquid to be extracted in which the component to be extracted is to be found, is separated from the liquid by gravity in a phase separator in which process in order to obtain an efficiency per extraction stage of at least 0.9 at an average residence time of at most 15 seconds in the dispersion apparatus and of at most 300 seconds in the phase separator, at a linear velocity in the coalescer related to its cross-section of at least 30 m/hour: a. the dispersion apparatus used is a centrifugal pump which will give droplets having an average diameter of 5 to 500 &mgr;m, b. the coalescer used is a packed bed of 5-100 cm high composed of dimensionally stable particles wettable by the extraction liquid having an average particle size of 0.05 to 2 mmL and c. the coagulated phase in the phase separator is separated at a linear velocity related to the cross-section of the phase separator of 0.1 to 0.7 times the linear velocity in the coalescer.
摘要翻译：本发明提供了一种通过使用与液体不混溶或仅部分混溶的萃取液的液 - 液萃取来提取溶解在液体中的组分的方法和装置，在该方法中，萃取液在液体中分散在液体中分散装置，然后在聚结器中聚结，之后其比重与要提取的组分的待提取液体的比重相差至少5％的前牵引液体为在相分离器中通过重力与液体分离，其中在分散装置中，为了在分散装置中平均停留时间至多为15秒，并且在相分离器中至多300秒，每个萃取阶段获得至少0.9的效率在与聚结器相关的线速度至少为30m /小时的横截面上：a。使用的分散装置是一种离心泵，其将产生平均直径为5至500μm的液滴，b。所使用的聚结器是由平均粒径为0.05-2mmL的萃取液可湿化的尺寸稳定的颗粒组成的5-100cm高的填充床。相分离器中的凝固相以与分离器的横截面相关的线速度分离成聚结器中的线速度的0.1至0.7倍。

10. 发明授权

US09487710B2 Process for producing at least one product from at least one gaseous reactant in a slurry bed 有权
标题翻译：用于在淤浆床中从至少一种气态反应物生产至少一种产物的方法
公开(公告)号：US09487710B2
公开(公告)日：2016-11-08
申请号：US14123994
申请日：2012-05-30
申请人： Berthold Berend Breman
发明人： Berthold Berend Breman
IPC分类号： C10G2/00 , B01J8/18 , B01J8/22 , B01J8/28
CPC分类号： C10G2/32 , B01J8/1827 , B01J8/1836 , B01J8/22 , B01J8/28 , B01J2208/00141 , B01J2208/00274 , C10G2/332 , C10G2/342 , Y02P20/582
摘要： A process for producing at least one product from at least one gaseous reactant includes feeding the gaseous reactant, as a gaseous feed or as part of a gaseous feed which is at an inlet superficial gas velocity of at least 0.5 m/s, into a vessel holding an expanded slurry bed of solid catalyst particles suspended in a suspension liquid so that the gaseous reactant can bubble upwardly through the slurry bed. The slurry bed has a catalyst loading of at least 20% by volume of degassed slurry. The gaseous reactant is allowed to react catalytically at a pressure above atmospheric pressure as the gaseous reactant bubbles upwardly through the slurry bed to produce at least one product. The product and any unreacted gaseous reactant are withdrawn from the vessel.
摘要翻译：用于从至少一种气态反应物生产至少一种产物的方法包括将气态反应物作为气态进料或作为入口表观气体速度为至少0.5m / s的气态进料的一部分进料到容器保持悬浮在悬浮液中的固体催化剂颗粒的膨胀淤浆床，使得气态反应物可以向上通过淤浆床。浆料床具有至少20体积％的脱气浆料的催化剂负载量。使气态反应物在高于大气压的压力下催化反应，因为气态反应物向上流过浆料床，以产生至少一种产物。将产物和任何未反应的气态反应物从容器中取出。

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