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1. 发明申请

US20040071618A1 Method and apparatus for continuously feeding and pressurizing a solid material into a high pressure system 有权
标题翻译：将固体材料连续进料和加压成高压系统的方法和装置
公开(公告)号：US20040071618A1
公开(公告)日：2004-04-15
申请号：US10271950
申请日：2002-10-15
发明人： Kenneth Michael Sprouse , David R. Matthews , Albert E. Stewart
IPC分类号： B01J008/08
CPC分类号： C10J3/50 , C10J2200/156 , C10J2300/0969
摘要： A system for substantially continuously providing a solid material, for example pulverized coal, to a pressurized container. The system provides the solid material to a first container of a first pressure elevated above an initial pressure of the solid material. Generally, a screw conveyor augmented with a jet port is used to move the material where the jet port provides a gas to provide a make-up volume of the solid material. The system also provides the material to a second high pressure container after the material has been formed into a slurry. Therefore, the solid material may be substantially continuously provided in a system to a high pressure container.
摘要翻译：一种用于将固体材料（例如粉煤）基本上连续地提供给加压容器的系统。该系统将固体材料提供给第一容器，该第一容器升高到高于固体材料的初始压力。通常，用喷射口增加的螺旋输送器用于移动喷射口提供气体的材料，以提供固体材料的补充体积。在材料已经形成浆料之后，该系统还将材料提供给第二高压容器。因此，固体材料可以基本上连续地设置在高压容器的系统中。

2. 发明申请

US20040024276A1 Two stage hydrocarbon conversion reaction system 有权
标题翻译：两阶段烃转化反应体系
公开(公告)号：US20040024276A1
公开(公告)日：2004-02-05
申请号：US10210217
申请日：2002-08-01
发明人： Jeffrey S. Smith , Keith Holroyd Kuechler , Nicolas P. Coute , Rathna P. Davuluri , David C. Skouby
IPC分类号： C07C001/00 , B01J008/08 , B01J008/00
CPC分类号： C10G3/62 , C10G3/49 , C10G2300/4018 , C10G2300/4093 , C10G2400/20 , Y02P30/20 , Y02P30/42
摘要： This invention is to a method and system for operating a hydrocarbon conversion process. A two stage reactor system is used in which the gas superficial velocity of the second reaction stage is greater than that in the first reaction stage. The first reaction stage operates at more continuous stirred tank reactor (CSTR) like characteristics, and the second reaction stage operates at more plug flow reactor (PFR) like characteristics.
摘要翻译：本发明是用于操作烃转化方法的方法和系统。使用两级反应器系统，其中第二反应级的气体表观速度大于第一反应级中的气体表观速度。第一反应阶段在更连续的搅拌釜反应器（CSTR）的特性下操作，第二反应阶段在更多的活塞流反应器（PFR）的特性下操作。

3. 发明申请

US20020068027A1 Fouling tolerant fixed bed reactor with multi-tier bypass device 失效
标题翻译：具有多层旁路装置的防污固定床反应器
公开(公告)号：US20020068027A1
公开(公告)日：2002-06-06
申请号：US09933939
申请日：2001-08-22
发明人： Ramesh Gupta , Salvatore Joseph Rossetti
IPC分类号： B01J008/02 , B01J008/08
CPC分类号： C10G49/002 , B01J8/008 , B01J8/025 , B01J8/0278 , B01J2208/00707
摘要： The invention is directed to a multi-tier bypass apparatus for extending the operating life of fixed bed reactors. The multi-tier bypass may be disposed within a fixed catalyst bed to allow any fluid feedstock to bypass successive layers of the fixed catalyst bed as they foul. The invention also relates to an improved fixed bed reactor comprising the inventive multi-tier bypass and a method for extending the operating life of a fixed bed reactor.
摘要翻译：本发明涉及一种用于延长固定床反应器的使用寿命的多层旁路装置。多层旁路可以设置在固定的催化剂床内，以允许任何流体原料在它们弄脏时绕过固定催化剂床的连续层。本发明还涉及一种改进的固定床反应器，其包括本发明的多层旁路和延长固定床反应器的使用寿命的方法。

4. 发明申请

US20020034464A1 Dry catalyst feeder for polymerization reactors 审中-公开
标题翻译：用于聚合反应器的干式催化剂进料器
公开(公告)号：US20020034464A1
公开(公告)日：2002-03-21
申请号：US09956673
申请日：2001-09-20
申请人： EQUISTAR CHEMICALS, L.P.
发明人： Thomas A. Glenn , Nadim F. Yaacoub , Joel A. Mutchler , Charles S. Holland , Dennis D. Gottschalk
IPC分类号： B01J008/08
CPC分类号： C08F10/00 , B01J8/0035 , C08F2/01 , C08F2/14
摘要： A device and method allow a dry catalyst to be delivered to a liquid-filled polymerization reactor, thus avoiding problems associated with catalyst-liquid contact or with undesired addition of gases to the reactor. A quantity of dry catalyst is transferred from a catalyst reservoir maintained under dry conditions to a catalyst chamber. An inert fluid then enters the chamber to flush the catalyst charge toward the reactor. Optional embodiments include means for precontacting the dry catalyst with a modifier and for removing gas from the fluid line.
摘要翻译：装置和方法允许将干燥的催化剂输送到充满液体的聚合反应器中，从而避免与催化剂 - 液体接触或不希望的向反应器中加入气体相关的问题。一定量的干燥催化剂从保持在干燥条件下的催化剂储存器转移到催化剂室。惰性流体然后进入室以将催化剂装料冲向反应器。可选的实施方案包括用于将干燥催化剂与改性剂预接触并用于从流体管线去除气体的装置。

5. 发明申请

US20020031459A1 FOULING TOLERANT FIXED BED REACTOR (LAW858) 审中-公开
标题翻译：防爆固定床反应器（LAW858）
公开(公告)号：US20020031459A1
公开(公告)日：2002-03-14
申请号：US09351648
申请日：1999-07-13
发明人： RAMESH GUPTA , SALVATORE JOSEPH ROSSETTI , DAVID CHARLES DANKWORTH , JEFFREY L. KAUFMAN , DAVID LEE VANNAUKER , JAMES PHILIP BAILOR
IPC分类号： B01J008/08
CPC分类号： B01J8/008 , B01J8/025 , B01J8/0278 , B01J2208/00707 , C10G49/002
摘要： The invention is directed to a reactor for reacting a feedstock, said reactor comprising, a fixed catalyst bed for reaction of said feedstock said reactor containing a bypass apparatus disposed within said fixed catalyst bed, said bypass apparatus being aligned with the direction of flow of said feedstock, and wherein said bypass apparatus comprise a cage member comprising a first elongated hollow member having a top wall, sidewalls and a bottom wall, said cage member having openings therein, and a second hollow elongated member for passing said feedstock therethrough, said second hollow elongated member being disposed within and protruding through said top wall of said cage member and wherein said second elongated member extends above said catalyst bed through said cage member.
摘要翻译：本发明涉及一种用于使原料反应的反应器，所述反应器包括用于使所述原料反应的固定催化剂床，所述反应器包含设置在所述固定催化剂床内的旁路装置，所述旁路装置与所述并且其中所述旁路装置包括保持架构件，所述保持架构件包括具有顶壁，侧壁和底壁的第一细长中空构件，所述保持架构件在其中具有开口，以及用于使所述原料通过其中的第二中空细长构件，细长构件设置在所述保持架构件的所述顶壁内并通过所述保持架构件的顶壁突出，并且其中所述第二细长构件在所述催化剂床的上方延伸穿过所述笼构件。

6. 发明申请

US20010043893A1 Continuous hydrosilylation method for production of a modified liquid organosilicon compound 有权
标题翻译：用于生产改性液体有机硅化合物的连续氢化硅烷化方法
公开(公告)号：US20010043893A1
公开(公告)日：2001-11-22
申请号：US09780074
申请日：2001-02-09
发明人： Toshio Okuyama , Naoya Matsui , Takao Takemasa
IPC分类号： B01J008/08
CPC分类号： C08G77/06 , B01J19/1862 , B01J19/20 , B01J2219/00094 , B01J2219/00103 , B01J2219/00779 , B01J2219/182 , C08G77/12 , C08G77/20 , C08L83/04 , C08L83/00
摘要： A continuous method for performing a hydrosilylation reaction comprising effecting a hydrosilylation reaction between a liquid organosilicon compound (A) having in each molecule at least one silicon-bonded hydrogen atom and a liquid organosilicon compound (B) having in each molecule at least one aliphatic unsaturated bond in the presence of a platinum catalyst (C) continuously in a tubular reactor equipped with a stirring and plug-flow maintaining apparatus located within the reactor.
摘要翻译：一种用于进行氢化硅烷化反应的连续方法，包括在每个分子中具有至少一个与硅键合的氢原子的液体有机硅化合物（A）和在每个分子中具有至少一个脂族不饱和基团的液体有机硅化合物（B）之间进行氢化硅烷化反应在配备有位于反应器内的搅拌和插塞流维持装置的管式反应器中，在铂催化剂（C）存在下连接。

7. 发明申请

US20040005254A1 Reactor for producing a nitrile compound and method for operating the reactor 审中-公开
标题翻译：用于生产腈化合物的反应器和操作反应器的方法
公开(公告)号：US20040005254A1
公开(公告)日：2004-01-08
申请号：US10326056
申请日：2002-12-23
发明人： Shuichi Ueno , Takuji Shitara , Kenichi Nakamura , Fumisada Kosuge
IPC分类号： B01J008/08 , C07D213/84 , C07C253/28
CPC分类号： F28D13/00 , B01J8/0055 , B01J8/1836 , B01J2208/00132 , B01J2208/00725 , C07C253/28 , C07C255/51
摘要： A reactor for producing a nitrile compound from a carbon ring or heterocyclic compound having organic substituents by a gas phase reaction using a fluidized catalyst bed with ammonia and a gas containing oxygen. In a cylindrical fluidized catalyst bed having a diameter of 2.0 meters or greater, partial vaporization-type cooling tubes (the cooling medium is partially vaporized in the tubes) and complete vaporization-type cooling tubes (the cooling medium is completely vaporized in the cooling tubes) are disposed in a specific arrangement. Water containing ionic SiO2 in 0.1 ppm or smaller and having an electric conductivity of 5 nullS/cm or smaller is used as the cooling medium for the complete vaporization-type cooling tubes. The temperature of the reaction is easily stabilized and uniform distribution of temperature is obtained in the fluidized catalyst bed. Stable continuous operation is achieved for a long time in a commercial scale apparatus.
摘要翻译：一种反应器，其由具有有机取代基的碳环或杂环化合物通过气相反应使用流化催化剂床与氨和含氧气体制备。在直径为2.0米或更大的圆柱形流化催化剂床中，部分气化型冷却管（冷却介质在管中部分蒸发）和完全蒸发式冷却管（冷却介质在冷却管中完全汽化）以特定的布置处理。使用0.1ppm以下的导电率为5μS/ cm以下的离子性SiO 2的水作为完全蒸发式冷却管的冷却介质。反应的温度容易稳定，在流化催化剂床中得到均匀的温度分布。在商业规模的设备中长期实现稳定的连续操作。

8. 发明申请

US20030211017A1 Resid cracking apparatus with catalyst and adsorbent regenerators and a process thereof 有权
标题翻译：具有催化剂和吸附剂再生器的残余裂解装置及其工艺
公开(公告)号：US20030211017A1
公开(公告)日：2003-11-13
申请号：US10140364
申请日：2002-05-08
发明人： Kawliwal Pankaj , Rama Rao Marri , Dixit Jagdev Kumar , Saroya Latoor Lal , Sukumar Mandal , Satish Makhija , Sobhan Ghosh
IPC分类号： B01J008/08 , B01J008/18
CPC分类号： C10J3/78 , C10G2300/107 , C10J3/482 , C10J3/54 , C10J2300/0916 , C10J2300/0973 , Y02P20/584
摘要： This invention provides a resid cracking apparatus comprising a riser, reactor, stripper cum separator with adjustable outlets in flow communication with adsorbent and catalyst regenerators for converting hydrocarbon residues containing higher concentration of conradson carbon content, poisonous metals such as nickel & vanadium and basic nitrogen etc., into lighter and valuable products and a process thereof.
摘要翻译：本发明提供了一种渣油裂解装置，其包括提升管，反应器，汽提器和分离器，其具有与吸附剂流动连通的可调节出口和用于转化含有较高浓度的康氏子碳含量的烃残余物的催化剂再生器，有毒金属如镍和钒和碱性氮等成为更轻和有价值的产品及其过程。

9. 发明申请

US20030129097A1 Fluidizing reactor and method of treatment of fluids 审中-公开
标题翻译：流化反应器和流体处理方法
公开(公告)号：US20030129097A1
公开(公告)日：2003-07-10
申请号：US10281636
申请日：2002-10-28
申请人： Marine Biotech Incorporated
发明人： Neil Helwig
IPC分类号： B01J008/18 , B01J008/08 , B01J008/12
CPC分类号： C02F3/085 , B01J8/1818 , B01J8/20 , Y02W10/15
摘要： A fluidizing reactor for treatment of fluid is provided. The fluidizing reactor includes an elongated column having an interior chamber extending between a first end and a second end of the column. The reactor also includes a plenum situated circumferentially about the second end of the column, and an inlet tangentially positioned relative to plenum, so as to introduce fluid to be treated into the plenum. The tangential position of the inlet imparts to the fluid a uniform cyclonic flow pattern circumferentially about the column. The reactor further includes an annulus about the second end of the column to provide an opening through which fluid from the plenum may enter into the interior chamber. Fluid flowing through the annulus is uniformly distributed into the interior chamber and maintains a cyclonic flow pattern. A fluid treatment material may be provided to treat the fluid flowing into the interior chamber.
摘要翻译：提供了一种用于处理流体的流化反应器。流化反应器包括具有在柱的第一端和第二端之间延伸的内室的细长柱。反应器还包括围绕塔的第二端周向定位的增压室和相对于增压室切向定位的入口，以将待处理的流体引入通风室。入口的切向位置向流体施加围绕柱的周向均匀的气旋流动模式。反应器还包括围绕塔的第二端的环形空间，以提供开口，通过该开口，来自气室的流体可以通过该开口进入内部室。流经环形空气的流体均匀地分布到内部腔室中，并保持气流模式。可以提供流体处理材料来处理流入室内的流体。

10. 发明申请

US20030124034A1 Catalytic cracking reaction-regeneration system 失效
标题翻译：催化裂化反应再生系统
公开(公告)号：US20030124034A1
公开(公告)日：2003-07-03
申请号：US10304748
申请日：2002-11-27
申请人： CHINA PETROLEUM & CHEMICAL CORPORATION
发明人： Xuefeng Wu , Jun He , Zhanfeng Zhang , Xianglin Yu , Xiaoxiang Zhong
IPC分类号： B01J008/08
CPC分类号： B01J8/0055 , B01J8/228 , B01J8/26 , C10G11/18 , C10G11/182
摘要： A catalytic cracking reaction-regeneration system, comprising a regenerator, a settler, a gas-solid separator, a buffer, a riser reactor, a horizontal reaction tube, a catalyst delivery pipe, and a down-flow reactor. This system can be used for experiments and researches on various processes such as riser catalytic cracking, sectional feeding, instantaneous contact, and down-flow catalytic cracking and can be used for catalyst evaluation tests. This abstract is neither intended to define the invention disclosed in this specification nor intended to limit the scope of the invention in any way.
摘要翻译：催化裂化反应再生系统，包括再生器，沉降器，气固分离器，缓冲器，提升管反应器，水平反应管，催化剂输送管和下流反应器。该系统可用于提升式催化裂化，分段进料，瞬时接触和下流催化裂化等各种工艺的实验和研究，可用于催化剂评价试验。该摘要既不旨在限定本说明书中公开的发明，也不旨在以任何方式限制本发明的范围。

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