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公开(公告)号：US4187169A
公开(公告)日：1980-02-05
申请号：US885222
申请日：1978-03-10
摘要： Liquid and gas materials are reacted in the presence of a catalyst in a reactor of the dispersed bed type which comprises a plurality of superposed chambers through which the catalyst progressively drops, its rate of transfer from one chamber to another being controlled by injecting an auxiliary fluid into downcomers through which the catalyst is forced to pass.
摘要翻译： 液体和气体材料在催化剂存在下在分散床型反应器中反应，该反应器包括多个重叠室，催化剂通过该反应器逐渐下降，其通过注入辅助流体来控制从一个室到另一个室的转移速率 进入催化剂被迫通过的降液管。
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公开(公告)号：US5772044A
公开(公告)日：1998-06-30
申请号：US508459
申请日：1995-07-28
CPC分类号： B07B13/003 , B07B1/06
摘要： An apparatus is provided for concentrating fine or broken particles to separate a particle stream into at least one stream which is concentrated in fine or broken particles and at least one stream with a reduced concentration of fine or broken particles. In addition to introduction and extraction structure, the apparatus includes at least two separator stages each comprising at least one funnel with an inclined or substantially vertical axis which opens upwardly, located beneath an inlet to collect the particles. The funnel is connected to at least one deflector which is directed downwardly to allow particles to flow under gravity and to form a bank of particles at the level of the funnel.
摘要翻译： 提供了一种用于浓缩精细或破碎的颗粒以将颗粒物流分离成至少一个流中的至少一个流，所述至少一个流被精细或破碎的颗粒和至少一个具有降低的细颗粒或破碎颗粒浓度的物流。 除了引入和提取结构之外，该装置还包括至少两个分离器级，每个分离器级包括至少一个漏斗，其具有向上开口的倾斜或基本上垂直的轴，位于入口下方以收集颗粒。 漏斗连接到至少一个导向器，该导流板被向下引导以允许颗粒在重力作用下流动并在漏斗的水平面上形成一束颗粒。
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公开(公告)号：US5658539A
公开(公告)日：1997-08-19
申请号：US506038
申请日：1995-07-24
CPC分类号： B01J8/12 , C10G35/12 , B01J2219/1925 , B01J2219/1943
摘要： An enclosure in which there circulates a moving bed of solid particles (for example a moving-bed catalytic reactor such as a reforming reactor), is delimited in the enclosure by at least one grill. In the enclosure a fluid passes through the bed in a direction different from that of the flow of the assembly of the particles and issues from the bed by way of at least one grill. Disposed in the thickness of said bed in an intermediate wall (grill) such as to distribute the thrust forces produced by the fluid on the particles in the zones of the bed which are delimited in that way. Jamming of the particles against the grill or grills is greatly reduced and the admissible fluid flow rate is then decreased.
摘要翻译： 在其中循环固体颗粒的移动床（例如移动床催化反应器例如重整反应器）的外壳通过至少一个格栅限定在外壳中。 在外壳中，流体沿与颗粒组件的流动不同的方向通过床，并通过至少一个格栅从床发出。 设置在中间壁（格栅）中的所述床的厚度上，以便将由流体产生的推力分配在以这种方式界定的床的区域中的颗粒上。 颗粒对格栅或烤架的干扰大大降低，然后允许的流体流速减小。
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公开(公告)号：US6090351A
公开(公告)日：2000-07-18
申请号：US148072
申请日：1998-09-04
申请人： Jean-Paul Euzen , Daniel Vuillemot , Roland Huin
发明人： Jean-Paul Euzen , Daniel Vuillemot , Roland Huin
CPC分类号： B01J8/0214 , B01J8/003 , B01J8/12 , C01B3/42 , C10G35/12 , B01J2208/00884 , B01J2219/1925 , B01J2219/1943 , C01B2203/0227
摘要： A chamber comprising a moving bed of solid particles, delimited by at least one screen with thickness e, circulating in a downward direction substantially parallel to the screen, the bed being traversed by at least one fluid flowing in the bed in a principal direction which is different to that of the ensemble of particles and leaving the bed by an outlet screen. In accordance with the invention, the chamber comprises at least one opening for introducing solid particles located above the bed and comprising at least one orifice for the flow of the particles, located at a distance of at least 0.6 e from the outlet screen. The chamber advantageously comprises at least two extraction openings, one extraction opening being located at a distance not more than 0.5 e from the outlet screen, and the other at a distance of at least 0.5 e from the outlet screen. The invention is applicable to catalytic reactors, in particular to catalytic reforming reactors.
摘要翻译： 一个室，包括固体颗粒的移动床，由至少一个具有厚度e的筛网限定，沿着基本上平行于筛网的向下方向循环，该床被沿着主要方向流过床的至少一种流体横穿， 不同于粒子的组合，并通过出口屏幕离开床。 根据本发明，腔室包括用于引入位于床上方的固体颗粒的至少一个开口，并且包括用于颗粒流动的至少一个孔口，该孔口与出口筛网距离至少0.6e。 所述室有利地包括至少两个提取开口，一个提取开口位于离出口屏幕不超过0.5埃的距离处，另一个距出口屏幕至少0.5埃的距离。 本发明适用于催化反应器，特别是催化重整反应器。
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公开(公告)号：US5833936A
公开(公告)日：1998-11-10
申请号：US642000
申请日：1996-05-02
CPC分类号： B01J8/0015 , B01J8/02 , B01J8/0214 , B01J8/12 , C10G35/12 , B01J2208/00761 , B01J2208/021 , B01J2219/1925 , B01J2219/1943
摘要： A vessel, in which a chemical reaction is carried out in the presence of a catalyst, comprises a bed (4) of solid catalytic particles, delimited by at least one wall (1, 10, 11) and a base (2). The base comprises at least one gravity extraction device (3) for the particles and a succession of ridges and hollows forming pleats. The ridges and hollows are oriented towards the extraction device. This succession is advantageously formed by an assembly of facets, which are preferably trapezoidal. The invention has particular application to mobile bed reactors, in particular those used for catalytic reforming of petroleum cuts.
摘要翻译： 在催化剂存在下进行化学反应的容器包括由至少一个壁（1,10,11）和碱（2）限定的固体催化剂颗粒床（4）。 底座包括用于颗粒的至少一个重力提取装置（3）和形成褶皱的一连串脊和中空部。 脊和凹槽朝向提取装置定向。 该连续性有利地由小平面的组合形成，其优选是梯形的。 本发明特别适用于移动床反应器，特别是用于石油馏分催化重整的反应器。
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6.发明授权Process for treating a hydrocarbon feed, comprising a counter-current fixed bed hydrotreatment step 有权用于处理烃进料的方法，包括逆流固定床加氢处理步骤公开(公告)号：US06645371B2
公开(公告)日：2003-11-11
申请号：US10022831
申请日：2001-12-20
IPC分类号： C10G4560
摘要： A process is described that can limit pressure drops during a catalytic hydrotreatment process carried out in a fixed bed reactor. The liquid feed and gaseous reactant are injected into the reactor either side of the bed and flow as a counter-current. Pressure drops are limited by homogeneously mixing solid catalytic and/or inert particles of different diameters in the bed.
摘要翻译： 描述了在固定床反应器中进行的催化加氢处理过程中可以限制压降的方法。 将液体进料和气体反应物注入床的两侧的反应器中并作为逆流流动。 通过在床中均匀混合不同直径的固体催化剂和/或惰性颗粒来限制压降。
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7.发明授权
公开(公告)号：US5302775A
公开(公告)日：1994-04-12
申请号：US831245
申请日：1992-02-07
CPC分类号： B04C7/00 , B01J8/005 , B01J8/1863 , B04C3/00 , B04C3/06 , C07C1/20 , Y02P20/584 , Y10S585/921 , Y10S585/922
摘要： Process for the catalytic conversion of a charge incorporating at least one oxygen compound such as methanol, into olefinic hydrocarbons having 2 to 4 carbon atoms. Conversion takes place in a reactor (100), into which the charge is introduced by the pipe (20), the catalytic solid by the pipe (30) and the solid entrainment gas by the pipe (40), the reactor being connected by a pipe (1) to a co-current cyclone separator (S) making it possible to separate a solid phase from a gaseous phase containing the conversion products, which is recovered by the pipe (4). The solid phase is fed by the pipe (9) to a regenerator (R), in which the catalytic particles are at least partly regenerated before being returned by the pipe (80), connected to the pipe (30), to the reactor (100).
摘要翻译： 将含有至少一种氧化合物如甲醇的电荷催化转化成具有2至4个碳原子的烯烃的方法。 在反应器（100）中进行转化，反应器（100）通过管道（20）引入电荷，通过管道（30）引入催化剂固体，通过管道（40）引入固体夹带气体，反应器由 管道（1）连接到并流旋风分离器（S），使得可以将固相从含有由管道（4）回收的转化产物的气相分离。 固相由管道（9）供给到再生器（R），其中催化剂颗粒在被连接到管道（30）的管道（80）返回到反应器之前被至少部分地再生 100）。
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8.发明授权
公开(公告)号：US5264645A
公开(公告)日：1993-11-23
申请号：US848599
申请日：1992-03-09
CPC分类号： B04C7/00 , B01J19/2405 , B04C3/00 , B04C3/06 , C07C1/20 , B01J2208/00557 , Y02P30/42 , Y10S585/921
摘要： The conversion of a charge comprising at least one oxygen compound is performed in a reactor C, into which the charge is introduced by the pipe (11), the solid catalytic particles forming the dense phase D1 by the pipe (14) and the solid entrainment gas by the pipe (12). The reactor is connected by a pipe (1) to a cocurrent cyclone separator-mixer (MS) making it possible to separate a solid phase from a gaseous phase containing the conversion products recovered by the pipe (4'), while carrying out a quenching of said gaseous phase by a product M2 introduced by the pipe (3). The phase D1 is fed by the pipe (7) to a regenerator R before being returned by the pipe (13) into the reactor C. The mixture of the gaseous phase and the product M2 is separated in a separator and the product M2, optionally after cooling, is recycled to the mixer-separator (MS).
摘要翻译： 包含至少一种氧化合物的电荷的转化在反应器C中进行，电荷通过管道（11）引入电荷，通过管道（14）形成密相D1的固体催化剂颗粒和固体夹带 气体通过管道（12）。 反应器通过管道（1）连接到并流旋风分离器 - 混合器（MS），使得可以将固相从含有由管道（4'）回收的转化产物的气相分离，同时进行淬火 的所述气相由管（3）引入的产物M2。 在由管道（13）返回到反应器C之前，相D1由管道（7）供给到再生器R。气相和产物M2的混合物在分离器中分离，产物M2，任选地 冷却后，再循环到混合器分离器（MS）中。
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