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1. 发明申请

US20090261046A1 FILTRATION METHOD AND INSTALLATION 有权
标题翻译：过滤方法和安装
公开(公告)号：US20090261046A1
公开(公告)日：2009-10-22
申请号：US12089197
申请日：2006-10-02
申请人： Ockert Rudolph Minnie , Patrick Otto Taylor , Pal Soraker , Marcus Fathi
发明人： Ockert Rudolph Minnie , Patrick Otto Taylor , Pal Soraker , Marcus Fathi
IPC分类号： B01D29/62
CPC分类号： B01J8/22 , B01J8/006 , B01J8/228 , C10G2/342
摘要： The invention provides a method for the separation of liquid from a three phase slurry bubble column. The method includes the step of charging the inside of a hollow filter element with a rinsing fluid to clean the inside of the filter for catalyst fines followed by a backflushing step. The invention also provides an installation for the separation of liquid from a three phase slurry bubble column. The installation includes at least one hollow and enclosed filter element and one or more conduits in fluid communication with the internal volume of filter, with at least one conduit being configured or connected for inflow of rinsing fluid and at least one conduit being configured or connected for outflow of rinsing fluid.
摘要翻译：本发明提供了一种从三相浆液气泡塔分离液体的方法。该方法包括用冲洗流体填充中空过滤元件的内部以清洁过滤器内部的催化剂细粒，随后进行反冲洗步骤的步骤。本发明还提供了用于从三相浆料气泡塔分离液体的装置。该安装包括至少一个中空和封闭的过滤器元件以及与过滤器的内部容积流体连通的一个或多个管道，至少一个导管被构造或连接用于冲洗流体的流入，并且至少一个导管被配置或连接用于冲洗液流出。

2. 发明授权

US09039980B2 Slurry bubble column reactor 有权
标题翻译：浆液鼓泡塔反应器
公开(公告)号：US09039980B2
公开(公告)日：2015-05-26
申请号：US13130041
申请日：2009-11-10
申请人： Manfred Ruppel , Thomas Gutermuth , Dag Schanke , Pal Soraker
发明人： Manfred Ruppel , Thomas Gutermuth , Dag Schanke , Pal Soraker
IPC分类号： B01J8/22 , C07C1/04 , C10G2/00 , B01J8/18
CPC分类号： B01J8/22 , B01J8/1818 , B01J8/224 , B01J8/226 , B01J2208/00911 , C07C1/0415 , C10G2/344
摘要： A slurry bubble column reactor with a gas distribution arrangement comprising an upper sparger, a lower sparger, and an open-ended tube. Gas from the lower sparger enters the tube and lowers the density of slurry in the tube. The difference in slurry density causes the slurry in the tube to rise, causing slurry outside the tube to move down, maintaining circulation and flushing catalyst from the vessel wall.
摘要翻译：一种具有气体分配装置的浆液鼓泡塔反应器，包括上喷射器，下喷射器和开口管。来自下部分布器的气体进入管并降低管中浆料的密度。浆料密度的差异导致管中的浆料升高，导致管外的浆料向下移动，保持从容器壁的循环和冲洗催化剂。

3. 发明申请

US20110313063A1 APPARATUS AND METHOD FOR CONDUCTING A FISCHER-TROPSCH SYNTHESIS REACTION 有权
标题翻译：用于诱导FISCHER-TROPSCH合成反应的装置和方法
公开(公告)号：US20110313063A1
公开(公告)日：2011-12-22
申请号：US13140384
申请日：2009-12-08
申请人： Pal Soraker , Manfred Ruppel , Dag Schanke , Matthias Wagner
发明人： Pal Soraker , Manfred Ruppel , Dag Schanke , Matthias Wagner
IPC分类号： C07C1/04 , B01J8/20
CPC分类号： C07C1/041 , B01J8/006 , B01J8/22 , B01J8/228 , C10G2/32 , C10G2/342 , C10G2/344
摘要： A system for a Fischer-Tropsch synthesis using a three-phase reactor in which a primary filter removes coarse catalyst particles from the product and in which catalyst fines are removed in a secondary filter. Some or all portion of the product wax from the secondary filter can be recycled back to the reactor, either as a back flush medium for the primary filter or directly to the slurry in the reactor, whereby removal of catalyst fines is rendered independent of the rate of wax production.
摘要翻译：使用三相反应器的费 - 托合成系统，其中初级过滤器从产物中除去粗催化剂颗粒，并且在二级过滤器中除去催化剂细粒。来自二级过滤器的产品蜡的一些或全部部分可以循环回到反应器中，作为用于初级过滤器的反冲洗介质或者直接反应到反应器中的浆料，从而使得催化剂细粒的除去与速率无关的蜡生产。

4. 发明授权

US09278891B2 Apparatus and method for conducting a fischer-tropsch synthesis reaction 有权
标题翻译：用于进行费 - 托合成反应的装置和方法
公开(公告)号：US09278891B2
公开(公告)日：2016-03-08
申请号：US13140384
申请日：2009-12-08
申请人： Pal Soraker , Manfred Ruppel , Dag Schanke , Matthias Wagner
发明人： Pal Soraker , Manfred Ruppel , Dag Schanke , Matthias Wagner
IPC分类号： B01J8/22 , C10G2/00 , C07C1/04 , B01J8/00
CPC分类号： C07C1/041 , B01J8/006 , B01J8/22 , B01J8/228 , C10G2/32 , C10G2/342 , C10G2/344
摘要： A system for a Fischer-Tropsch synthesis using a three-phase reactor in which a primary filter removes coarse catalyst particles from the product and in which catalyst fines are removed in a secondary filter. Some or all portion of the product wax from the secondary filter can be recycled back to the reactor, either as a back flush medium for the primary filter or directly to the slurry in the reactor, whereby removal of catalyst fines is rendered independent of the rate of wax production.
摘要翻译：使用三相反应器的费 - 托合成系统，其中初级过滤器从产物中除去粗催化剂颗粒，并且在二级过滤器中除去催化剂细粒。来自二级过滤器的产品蜡的一些或全部部分可以循环回到反应器中，作为用于初级过滤器的反冲洗介质或者直接反应到反应器中的浆料，由此除去催化剂细粒以使其与速率无关的蜡生产。

5. 发明申请

US20110313062A1 SLURRY BUBBLE COLUMN REACTOR 有权
标题翻译：浆液泡沫反应器
公开(公告)号：US20110313062A1
公开(公告)日：2011-12-22
申请号：US13130041
申请日：2009-11-10
申请人： Manfred Ruppel , Thomas Gutermuth , Dag Schanke , Pal Soraker
发明人： Manfred Ruppel , Thomas Gutermuth , Dag Schanke , Pal Soraker
IPC分类号： C07C27/00 , B01J19/00
CPC分类号： B01J8/22 , B01J8/1818 , B01J8/224 , B01J8/226 , B01J2208/00911 , C07C1/0415 , C10G2/344
摘要： A slurry bubble column reactor with a gas distribution arrangement comprising an upper sparger, a lower sparger, and an open-ended tube. Gas from the lower sparger enters the tube and lowers the density of slurry in the tube. The difference in slurry density causes the slurry in the tube to rise, causing slurry outside the tube to move down, maintaining circulation and flushing catalyst from the vessel wall.
摘要翻译：一种具有气体分配装置的浆液鼓泡塔反应器，包括上喷射器，下喷射器和开口管。来自下部分布器的气体进入管并降低管中浆料的密度。浆料密度的差异导致管中的浆料升高，导致管外的浆料向下移动，保持从容器壁的循环和冲洗催化剂。

6. 发明授权

US5997826A Reactor for catalytic dehydrogenation of hydrocarbons with selective oxidation of hydrogen 失效
标题翻译：用氢气选择性氧化的催化脱氢反应器
公开(公告)号：US5997826A
公开(公告)日：1999-12-07
申请号：US860069
申请日：1997-08-05
申请人： Rune Lodeng , Pal Soraker
发明人： Rune Lodeng , Pal Soraker
IPC分类号： B01J8/04 , C07C5/333 , C07C5/48 , B01J8/02 , B01J10/00 , B01J35/02
CPC分类号： B01J8/0492 , B01J8/04 , B01J8/0457 , C07C5/333 , C07C5/48
摘要： A reactor for catalytic dehydrogenation of dehydrogenatable hydrocarbons, in particular C.sub.3 and/or C.sub.4 hydrocarbons, in a hydrocarbon-containing stream, with selective oxidation of hydrogen. The reactor comprises serially connected in the flow direction of the hydrocarbon-containing stream: a first catalyst zone (2), an oxygen admixing zone (3) provided with a means (5) for separate feeding of an oxygen-containing gas into the hydrocarbon-containing stream, and a second catalyst zone (4). The oxygen admixing zone (3) has a cross section area in the flow direction of the hydrocarbon-containing stream which is from 0.5% to 75% of the cross section area of each of the two catalysts zones (2, 4), so as to obtain a higher flow velocity in the oxygen-admixing zone (3) than in the catalyst zones. The means (5) for feeding oxygen-containing gas is designed to feed said gas with a flow velocity which is at least 1 m/s and is up to 200 times higher than the flow velocity of the hydrocarbon-containing stream in the oxygen-admixing zone. The oxygen-admixing zone (3) is free of catalyst at least in the region adjacent to the oxygen feeding means (5).
摘要翻译： PCT No.PCT / NO95 / 00236 Sec。 371日期：1997年8月5日 102（e）日期1997年8月5日PCT 1995年12月18日PCT PCT。出版物WO96 / 19424 日期1996年6月27日一种用于在含烃流中催化脱氢可再氢化烃，特别是C3和/或C4烃的反应器，其具有氢的选择性氧化。反应器包括在含烃流的流动方向上串联连接：第一催化剂区（2），氧混合区（3），其设有用于将含氧气体单独进料到烃中的装置（5）和第二催化剂区（4）。氧混合区（3）在含烃流的流动方向上具有占两个催化剂区域（2,4）的截面积的0.5％至75％的横截面积，因此以在氧气混合区（3）中获得比在催化剂区域中更高的流速。用于供给含氧气体的装置（5）被设计成以至少1m / s的流速供给所述气体，并且比含氧气体中的含烃流的流速高达200倍。混合区至少在与氧气供给装置（5）相邻的区域中，氧气混合区（3）不含催化剂。

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