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1. 发明授权

US5643537A FCC process and apparatus with contained vortex third stage separator 失效
标题翻译： FCC工艺和装置含有涡流第三级分离器
公开(公告)号：US5643537A
公开(公告)日：1997-07-01
申请号：US533135
申请日：1995-09-26
申请人： Michael F. Raterman , Christopher G. Smalley
发明人： Michael F. Raterman , Christopher G. Smalley
IPC分类号： B04C9/00 , B01D45/12 , B01J8/00 , B04C5/00 , B04C5/081 , B04C5/14 , B04C5/187 , B04C5/28 , C10G11/18 , F27D17/00 , F27B15/09
CPC分类号： B01D45/12 , B01J8/0055 , B04C5/081 , B04C5/14 , B04C5/187 , B04C5/28 , C10G11/18
摘要： Vertical, small diameter cyclones are disclosed. Gas and fines are added tangentially or axially around a clean vapor outlet tube in a cylindrical cyclone. A vortex of solids and some gas passes into a contiguous and axially aligned cylindrical vortex containment means from which solids are withdrawn via a vertical slot in a sidewall of the containment means. 0-5 micron particle removal is enhanced. An FCC process uses the cyclones as a third stage separator.
摘要翻译：公开了垂直的，小直径的旋风分离器。气体和细屑在圆柱形旋风分离器中的干净蒸气出口管周围切向或轴向加入。固体和一些气体的涡流进入连续和轴向对准的圆柱形涡流容纳装置，固体通过容器装置的侧壁中的垂直槽排出。 0-5微米颗粒去除增强。 FCC工艺使用旋风分离器作为第三级分离器。

2. 发明授权

US5538696A FCC process and apparatus with contained vortex third stage separator 失效
标题翻译： FCC工艺和装置含有涡流第三级分离器
公开(公告)号：US5538696A
公开(公告)日：1996-07-23
申请号：US236975
申请日：1994-05-02
申请人： Michael F. Raterman , Christopher G. Smalley
发明人： Michael F. Raterman , Christopher G. Smalley
IPC分类号： B04C9/00 , B01D45/12 , B01J8/00 , B04C5/081 , B04C5/14 , B04C5/187 , B04C5/28 , C10G11/18 , F27B15/12
CPC分类号： C10G11/18 , B01D45/12 , B01J8/0055 , B04C5/081 , B04C5/14 , B04C5/187 , B04C5/28
摘要： Horizontal, small diameter cyclones are disclosed. Gas and fines are added tangentially around a clean vapor outlet tube in a cylindrical cyclone. A vortex of solids and some gas passes into a contiguous and axially aligned cylindrical vortex containment means from which solids are withdrawn via a horizontal slot. 0-5 micron particle removal is enhanced. An FCC process uses the cyclones as a third stage separator. An alternative design uses a half pipe extension on the solids outlet to confine the vortex of solids and gas.
摘要翻译：公开了水平的小直径旋风分离器。在圆柱形旋风分离器内的清洁蒸汽出口管周围，气体和细屑切向加入。固体和一些气体的涡流进入连续和轴向对准的圆柱形涡流容纳装置，固体通过水平槽从该容器中排出。 0-5微米颗粒去除增强。 FCC工艺使用旋风分离器作为第三级分离器。替代设计使用固体出口上的半管延伸部分限制固体和气体的涡流。

3. 发明授权

US5372707A Underflow cyclones and FCC process 失效
标题翻译：底流旋风和FCC工艺
公开(公告)号：US5372707A
公开(公告)日：1994-12-13
申请号：US047911
申请日：1993-05-28
申请人： J. Scott Buchanan , Michael F. Raterman , Christopher G. Smalley
发明人： J. Scott Buchanan , Michael F. Raterman , Christopher G. Smalley
IPC分类号： B04C5/10 , B04C5/14 , C10G11/18 , B01D21/26 , B01D45/12 , B04C1/00
CPC分类号： C10G11/18 , B04C5/10 , B04C5/14
摘要： A "leaking" cyclone and process for fluidized catalytic cracking of heavy oils is disclosed. Gas and entrained solids are added tangentially to swirl around a vapor outlet tube in a cylindrical tube cyclone body. A concentrated stream of solids and some gas is withdrawn from the device through openings in the cylindrical sidewall remote from the inlet. Tangential withdrawal via an offset slit in the sidewall, or withdrawal through holes in the sidewall, replaces or reduces conventional underflow of solids from an end of the cyclone body. Fine (0-5 micron) particles removal is enhanced by withdrawing solids as soon as solids reach the cylindrical sidewall. The device may be used as a third stage separator on an FCC regenerator.
摘要翻译：公开了一种“泄漏”旋风分离器和重油流化催化裂化方法。气体和夹带的固体被切向加入以在圆柱形管旋风器体内的蒸气出口管周围旋转。浓缩的固体物流和一些气体通过远离入口的圆柱形侧壁中的开口从装置中排出。通过侧壁中的偏移狭缝或侧壁中的孔抽出而进行切向取出，代替或减少了旋风体主体端部固体的常规下溢。一旦固体到达圆柱形侧壁，即可通过抽出固体来提高精细（0-5微米）的颗粒去除。该装置可以用作FCC再生器上的第三级分离器。

4. 发明授权

US09095831B2 Fluid bed reactor with staged baffles 有权
标题翻译：流化床反应器与分段挡板
公开(公告)号：US09095831B2
公开(公告)日：2015-08-04
申请号：US13557605
申请日：2012-07-25
申请人： Lu Han , Rathna P. Davuluri , Christopher G. Smalley , Mark P. Hagemeister , Masaaki Sugita , Joseph S. Famolaro , Robert G. Tinger
发明人： Lu Han , Rathna P. Davuluri , Christopher G. Smalley , Mark P. Hagemeister , Masaaki Sugita , Joseph S. Famolaro , Robert G. Tinger
IPC分类号： B01J8/18 , B01J8/34 , C07C2/86 , B01J8/00 , B01J8/24 , B01J19/32 , C07C2/54 , C07C2/56 , C07C2/58 , C07C2/64 , C07C2/66 , C07C15/00 , C07C15/02 , C07C15/04 , C07C15/06 , C07C15/08
CPC分类号： B01J8/34 , B01J8/1818 , B01J8/1827 , B01J8/1872 , C07C2/864 , C07C2/865 , Y02P20/52 , C07C15/08
摘要： The invention relates to a process of alkylating aromatic hydrocarbons, and more particularly a process of making paraxylene by alkylation of benzene and/or toluene with methanol and/or dimethyl ether, and to an apparatus for carrying out said process, the improvement comprising staged injection of one of the reactants, with the stages separated by structured packing so as to minimize at least one of gas phase back-mixing, by-pass phenomena, and gas bubble size.
摘要翻译：本发明涉及芳族烃的烷基化方法，更具体地说是一种通过用甲醇和/或二甲醚烷基化苯和/或甲苯来制备对二甲苯的方法，以及用于进行所述方法的设备，其改进包括分段注射其中一种反应物，其阶段由规整填料分离，以使气相回混，旁路现象和气泡尺寸中的至少一种最小化。

5. 发明申请

US20070251863A1 FCC catalyst stripper configuration 有权
标题翻译： FCC催化剂脱汽器配置
公开(公告)号：US20070251863A1
公开(公告)日：2007-11-01
申请号：US11729353
申请日：2007-03-28
申请人： Brian A. Cunningham , Christopher G. Smalley , Richard C. Senior , Joseph S. Famolaro , Rathna P. Davuluri , David L. Johnson , James H. Beech , Jeffrey S. Smith
发明人： Brian A. Cunningham , Christopher G. Smalley , Richard C. Senior , Joseph S. Famolaro , Rathna P. Davuluri , David L. Johnson , James H. Beech , Jeffrey S. Smith
IPC分类号： C10G11/02 , B01J8/24
CPC分类号： B01J8/0055 , B01J8/008 , B01J8/1818 , B01J8/1827 , B01J8/1872 , B01J8/26 , B01J8/34 , B01J8/388 , B01J2208/0084 , C10G11/182 , C10G2300/1033 , C10G2300/1044 , C10G2300/1059 , C10G2300/107 , C10G2300/1077 , C10G2300/4093 , C10G2400/20 , Y02P30/20
摘要： This invention relates to the catalytic cracking of a hydrocarbon feed. In particular, this invention relates to an apparatus and process utilizing a catalyst stripper section of a fluid catalytic cracking (FCC) reactor with chordal trays designed to provide improved stripping of hydrocarbons from spent FCC catalyst in an FCC reactor stripping zone.
摘要翻译：本发明涉及烃进料的催化裂化。特别地，本发明涉及一种使用流体催化裂化（FCC）反应器的催化剂汽提部分的装置和方法，其中弦杆塔设计成在FCC反应器汽提区中从废FCC催化剂提供改进的烃汽提。

6. 发明授权

US06248298B1 FCC unit catalyst stripper 失效
标题翻译： FCC单元催化剂汽提器
公开(公告)号：US06248298B1
公开(公告)日：2001-06-19
申请号：US08771869
申请日：1996-12-23
申请人： Richard C. Senior , Christopher G. Smalley , Timothy P. Holtan
发明人： Richard C. Senior , Christopher G. Smalley , Timothy P. Holtan
IPC分类号： F27B1508
CPC分类号： C10G11/18 , B01J8/0055 , B01J8/34
摘要： An improved stripper section design is provided for use in fluid catalytic cracking (FCC) units. The stripper section contains means for imparting rotational movement to the FCC cracking catalyst as it traverses the stripping section. In one embodiment the stripper section contains at least one rotation vane that is preferably disposed on the surface of a stripper section tray. The rotation vane provides angular, rotational movement to the cracking catalyst as it traverses the stripper section. Vertical movement is imparted to the cracking catalyst due to gravity and radial movement is imparted to the catalyst due to the slanted nature of the tray. Through the use of the rotation vanes the contact between the catalyst particles and the stripping steam is increased, thereby improving the overall efficiency of the FCC operation.
摘要翻译：提供了一种用于流化催化裂化（FCC）装置的改进的汽提部分设计。汽提器部分包含用于当FCC裂化催化剂穿过汽提部分时向FCC裂化催化剂施加旋转运动的装置。在一个实施例中，汽提器部分包含至少一个旋转叶片，其优选地设置在汽提器部分托盘的表面上。旋转叶片在穿过剥离器部分时向裂化催化剂提供角度旋转运动。由于重力而使裂纹催化剂产生垂直运动，并且由于托盘的倾斜性质，向催化剂施加径向移动。通过使用旋转叶片，催化剂颗粒和汽提蒸汽之间的接触增加，从而提高了FCC操作的总体效率。

7. 发明申请

US20090020454A1 Reduced elevation catalyst return line for a fluid catalytic cracking unit 有权
标题翻译：用于流化催化裂化装置的降低催化剂返回管路
公开(公告)号：US20090020454A1
公开(公告)日：2009-01-22
申请号：US11879259
申请日：2007-07-17
申请人： Brian A. Cunningham , Christopher G. Smalley , Rathna P. Davuluri , Dana W. Nouri
发明人： Brian A. Cunningham , Christopher G. Smalley , Rathna P. Davuluri , Dana W. Nouri
IPC分类号： C10G11/00 , B01D53/00
CPC分类号： B01J8/0015 , C10G11/18 , C10G11/182 , C10G2300/301
摘要： The present invention is an improved regenerated catalyst bend assembly for a fluid catalytic cracking unit. In a preferred embodiment, the reduced elevation (“RE-bend” or “REL-bend”) regenerated catalyst return line assembly of the present invention has an outlet elevation that is lower than the inlet elevation of the RE-bend or REL-bend regenerated catalyst return line assembly, and a process for utilizing the assembly in a fluid catalytic cracking unit. The present invention is especially useful in the modification of existing fluid catalytic cracking units to lower the elevation of the outlet of the regenerated catalyst return line assembly, thereby providing needed space to increase the fluid catalytic cracking reactor riser length.
摘要翻译：本发明是用于流化催化裂化装置的改进的再生催化剂弯曲组件。在优选实施例中，本发明的再生催化剂返回管线组件的缩小的高度（“RE-弯曲”或“REL-弯曲”）具有低于RE弯头或REL-弯头的入口高度的出口高度再生催化剂返回管路组件，以及在流化催化裂化装置中利用该组件的方法。本发明特别可用于改进现有的流化催化裂化装置以降低再生催化剂返回管线组件的出口的高度，从而提供所需的空间以增加流化催化裂化反应器提升管的长度。

8. 发明授权

US5514271A Underflow cyclone with perforated barrel 失效
标题翻译：底吹旋风筒带孔筒
公开(公告)号：US5514271A
公开(公告)日：1996-05-07
申请号：US234794
申请日：1994-04-28
申请人： John S. Buchanan , Christopher G. Smalley
发明人： John S. Buchanan , Christopher G. Smalley
IPC分类号： B01D45/12 , B01J8/00 , B04C5/081 , B04C5/10 , B04C5/14 , B04C5/28 , C10G11/18 , C01G11/00 , B04C3/06
CPC分类号： B04C5/10 , B01D45/12 , B01J8/0055 , B04C5/081 , B04C5/14 , B04C5/28 , C10G11/18
摘要： A cyclone and process for fluidized catalytic cracking of heavy oils is disclosed. Gas and entrained solids are added tangentially around a vapor outlet tube in a cylindrical tube cyclone body. Solids and some gas is withdrawn via a plurality of openings radially and longitudinally distributed in the cylindrical sidewall of the cyclone body. Distributed withdrawal replaces or reduces conventional underflow of solids from an end of cyclone outlet and reduces solids reentrainment. 0-5 micron particle removal is enhanced by reducing eddy formation and particle bouncing near the cyclone sidewall. The device may be used as an FCC regenerator third stage separator.
摘要翻译：公开了用于重油流化催化裂化的旋风分离器和方法。气体和夹带的固体围绕圆柱形管旋风器主体中的蒸气出口管切向加入。固体和一些气体通过径向和纵向分布在旋风器主体的圆柱形侧壁中的多个开口被排出。分布式抽出取代或减少了旋风出口端部固体的常规下溢，并减少了固体再吸入。通过减少旋风分离器侧壁附近的漩涡形成和颗粒弹跳来增强0-5微米的颗粒去除。该装置可用作FCC再生器第三级分离器。

9. 发明申请

US20130165724A1 Fluid Bed Reactor with Staged Baffles 有权
标题翻译：流化床反应堆与分级挡板
公开(公告)号：US20130165724A1
公开(公告)日：2013-06-27
申请号：US13557605
申请日：2012-07-25
申请人： Lu Han , Rathna P. Davuluri , Christopher G. Smalley , Mark Hagemeister , Masaaki Sugita , Joseph S. Famolaro , Robert G. Tinger
发明人： Lu Han , Rathna P. Davuluri , Christopher G. Smalley , Mark Hagemeister , Masaaki Sugita , Joseph S. Famolaro , Robert G. Tinger
IPC分类号： B01J8/18
CPC分类号： B01J8/34 , B01J8/1818 , B01J8/1827 , B01J8/1872 , C07C2/864 , C07C2/865 , Y02P20/52 , C07C15/08
摘要： The invention relates to a process of alkylating aromatic hydrocarbons, and more particularly a process of making paraxylene by alkylation of benzene and/or toluene with methanol and/or dimethyl ether, and to an apparatus for carrying out said process, the improvement comprising staged injection of one of the reactants, with the stages separated by structured packing so as to minimize at least one of gas phase back-mixing, by-pass phenomena, and gas bubble size.
摘要翻译：本发明涉及芳族烃的烷基化方法，更具体地说是一种通过用甲醇和/或二甲醚烷基化苯和/或甲苯来制备对二甲苯的方法，以及用于进行所述方法的设备，其改进包括分段注入其中一种反应物，其阶段由规整填料分离，以使气相回混，旁路现象和气泡尺寸中的至少一种最小化。

10. 发明授权

US07744746B2 FCC catalyst stripper configuration 有权
标题翻译： FCC催化剂脱汽器配置
公开(公告)号：US07744746B2
公开(公告)日：2010-06-29
申请号：US11729353
申请日：2007-03-28
申请人： Brian A. Cunningham , Christopher G. Smalley , Richard C. Senior , Joseph S. Famolaro , Rathna P. Davuluri , David L. Johnson , James H. Beech , Jeffrey S. Smith
发明人： Brian A. Cunningham , Christopher G. Smalley , Richard C. Senior , Joseph S. Famolaro , Rathna P. Davuluri , David L. Johnson , James H. Beech , Jeffrey S. Smith
IPC分类号： C10G11/02
CPC分类号： B01J8/0055 , B01J8/008 , B01J8/1818 , B01J8/1827 , B01J8/1872 , B01J8/26 , B01J8/34 , B01J8/388 , B01J2208/0084 , C10G11/182 , C10G2300/1033 , C10G2300/1044 , C10G2300/1059 , C10G2300/107 , C10G2300/1077 , C10G2300/4093 , C10G2400/20 , Y02P30/20
摘要： This invention relates to the catalytic cracking of a hydrocarbon feed. In particular, this invention relates to an apparatus and process utilizing a catalyst stripper section of a fluid catalytic cracking (FCC) reactor with chordal trays designed to provide improved stripping of hydrocarbons from spent FCC catalyst in an FCC reactor stripping zone.
摘要翻译：本发明涉及烃进料的催化裂化。特别地，本发明涉及一种使用流体催化裂化（FCC）反应器的催化剂汽提部分的装置和方法，其中弦杆塔设计成在FCC反应器汽提区中从废FCC催化剂提供改进的烃汽提。

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