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81. 发明申请

US20060037589A1 Heat pipe for heating of gasoline for on-board octane segregation 审中-公开
标题翻译：用于加热汽油用于板上辛烷值偏析的热管
公开(公告)号：US20060037589A1
公开(公告)日：2006-02-23
申请号：US11187672
申请日：2005-07-22
申请人： Ramesh Gupta , Sanjay Bhatia , George Walchuk , Randall Partridge , Walter Weissman
发明人： Ramesh Gupta , Sanjay Bhatia , George Walchuk , Randall Partridge , Walter Weissman
IPC分类号： F02G5/00 , F02B13/00
CPC分类号： F02M37/0064 , C10G31/11 , F02D19/0649 , F02D19/0671 , F02G5/02 , F02M1/165 , Y02T10/166 , Y02T10/36
摘要： In an internal combustion engine fuel system having a membrane separator for separating a primary fuel into a high octane fuel and a low octane fuel, and wherein the primary fuel is heated for separation in the membrane separator, the improvement comprising a heat pipe having an evaporator section positioned to be in the heat exchange relationship with exhaust gas from the internal combustion engine under conditions of use; and a heat output area in heat exchange relationship with a primary fuel as it is fed into the separator whereby the primary fuel is heated. In one embodiment the heat pipe is a variable conductance heat pipe having a top operating temperature not greater than about 160° C.
摘要翻译：在具有用于将初级燃料分离为高辛烷值燃料和低辛烷值燃料的膜分离器的内燃机燃料系统中，在膜分离器中加热主要燃料进行分离，其改进包括具有蒸发器的热管在使用条件下被定位成与来自内燃机的废气的热交换关系; 以及当其被馈送到隔板中时与主要燃料的热交换关系的热输出区域，由此主要燃料被加热。在一个实施例中，热管是可变电导热管，其顶部操作温度不大于约160℃

82. 发明申请

US20050204629A1 Combined water gas shift reactor/carbon dioxide adsorber for use in a fuel cell system 有权
标题翻译：用于燃料电池系统的组合式水煤气变换反应器/二氧化碳吸附器
公开(公告)号：US20050204629A1
公开(公告)日：2005-09-22
申请号：US10753024
申请日：2004-01-07
申请人： Craig Gittleman , Ramesh Gupta
发明人： Craig Gittleman , Ramesh Gupta
IPC分类号： B01D53/04 , B01D53/047 , B01D53/06 , B01D53/86 , C01B3/16 , C01B3/32 , C01B3/38 , C01B3/48 , C01B3/56 , H01M8/00 , H01M8/04 , H01M8/06 , H01M8/10 , B01D53/62 , C01B3/24
CPC分类号： B01D53/06 , B01D53/047 , B01D53/864 , B01D2253/102 , B01D2253/104 , B01D2253/108 , B01D2253/112 , B01D2256/16 , B01D2257/502 , B01D2257/504 , B01D2259/40052 , B01D2259/40062 , B01D2259/41 , C01B3/16 , C01B3/48 , C01B3/56 , C01B2203/0205 , C01B2203/0283 , C01B2203/0425 , C01B2203/047 , C01B2203/0475 , C01B2203/0495 , C01B2203/066 , C01B2203/0811 , C01B2203/0822 , C01B2203/0827 , C01B2203/0883 , C01B2203/1005 , C01B2203/1047 , C01B2203/1082 , C01B2203/1223 , C01B2203/1229 , C01B2203/1241 , C01B2203/1247 , C01B2203/146 , C01B2203/1604 , C01B2203/1652 , C01B2203/82 , H01M8/0612 , H01M8/0668 , Y02C10/08 , Y02P20/128 , Y02P20/129 , Y02P20/152
摘要： An apparatus removes CO from a hydrogen-rich gas stream in a hydrogen fuel cell system. CO fouls costly catalytic particles in the membrane electrode assemblies. Both a catalyst adapted to perform a water gas shift reaction, and a carbon dioxide adsorbent are disposed in a rotating pressure swing adsorber housing. The adsorption of carbon dioxide shifts equilibrium toward carbon monoxide consumption. A second adsorbent may be disposed in the housing for adsorbing carbon monoxide at low temperatures, and is adapted to desorb carbon monoxide at high temperatures. The present invention advantageously eliminates a unit operation from a space-constrained fuel cell vehicle by combining the WGS catalyst and a CO2 adsorbent in a single reactor/housing. The apparatus further eliminates the use of a PROX reactor, by providing an apparatus which incorporates CO2 adsorption and consequent carbon monoxide consumption in the place of the PROX reactor.
摘要翻译：一种装置从氢燃料电池系统中的富氢气流中除去CO。 CO会损坏膜电极组件中昂贵的催化颗粒。适用于执行水煤气变换反应的催化剂和二氧化碳吸附剂均设置在旋转变压吸附器壳体中。二氧化碳的吸附将平衡转移到一氧化碳消耗。第二吸附剂可以设置在壳体中用于在低温下吸附一氧化碳，并且适于在高温下解吸一氧化碳。本发明通过在单个反应器/壳体中组合WGS催化剂和CO 2 H 2吸附剂有利地消除了来自空间受限的燃料电池车辆的单元操作。该设备进一步消除了PROX反应器的使用，通过提供一种包含CO 2吸附和随后的一氧化碳消耗代替PROX反应器的装置。

83. 发明授权

US06241952B1 Countercurrent reactor with interstage stripping of NH3 and H2S in gas/liquid contacting zones 有权
标题翻译：逆流反应器，在气/液接触区域内具有级间汽提NH3和H2S
公开(公告)号：US06241952B1
公开(公告)日：2001-06-05
申请号：US09373255
申请日：1999-08-12
申请人： Edward S. Ellis , Ramesh Gupta
发明人： Edward S. Ellis , Ramesh Gupta
IPC分类号： B01J804
CPC分类号： C10G49/002 , B01J8/0492
摘要： A reactor for reacting liquid petroleum or chemical streams wherein the liquid stream flows countercurrent to the flow of a treat gas, such as a hydrogen-containing gas. The reactor is comprised of at least one vertically disposed reaction zone, each containing a bed of catalyst, wherein each reaction zone may contain vapor bypass means, and wherein each reaction zone is immediately preceded by a non-reaction zone, and wherein each non-reaction zone contains a gas/liquid contacting zone for stripping gaseous by-products, such as NH3 and H2S, from the liquid stream.
摘要翻译：用于使液体石油或化学物流反应的反应器，其中液体流与处理气体的流动例如含氢气体逆流流动。反应器由至少一个垂直设置的反应区组成，每个反应区各自含有催化剂床，其中每个反应区可以含有蒸气旁路装置，并且其中每个反应区紧接在非反应区之前，反应区包含用于从液体流中汽提气态副产物如NH 3和H 2 S的气/液接触区。

84. 发明授权

US6007787A Countercurrent reaction vessel 失效
标题翻译：逆流反应容器
公开(公告)号：US6007787A
公开(公告)日：1999-12-28
申请号：US702334
申请日：1996-08-23
申请人： Ramesh Gupta , David C. Dankworth , Dennis D. Fleming , Edward S. Ellis , James J. Schorfheide
发明人： Ramesh Gupta , David C. Dankworth , Dennis D. Fleming , Edward S. Ellis , James J. Schorfheide
IPC分类号： B01D3/16 , B01J8/04 , B01J19/24 , C10G45/00 , C10G45/44 , C10G47/00 , C10G49/00 , C10G65/02
CPC分类号： B01D3/16 , B01J8/0453 , B01J8/0492 , C10G49/002
摘要： A reaction vessel for processing liquid petroleum or chemical streams wherein the stream flows countercurrent to the flow of a treat gas, such as a hydrogen-containing gas, in at least one interaction zone. The reaction vessel contains vapor, and optionally liquid, passageways to bypass one or more packed beds, preferably catalyst beds. This permits more stable and efficient vessel operation.
摘要翻译：一种用于处理液体石油或化学物流的反应容器，其中所述流在至少一个相互作用区域中与处理气体（例如含氢气体）的流动逆流流动。反应容器含有蒸气和任选的液体，以绕过一个或多个填充床，优选催化剂床。这允许更稳定和高效的船只操作。

85. 发明授权

US5989411A Staged upflow hydroprocessing with noncatalytic impurity removal from the first stage vapor effluent 有权
标题翻译：从第一级蒸汽流出物中分离出非催化杂质，分阶段上流加氢处理
公开(公告)号：US5989411A
公开(公告)日：1999-11-23
申请号：US177735
申请日：1998-10-23
申请人： Ramesh Gupta
发明人： Ramesh Gupta
IPC分类号： C10G65/02 , C10G25/00 , C10G45/00 , C10G45/02 , C10G45/32 , C10G45/44 , C10G45/58 , C10G47/00 , C10G49/00 , C10G65/04 , C10G67/02 , C10G67/04 , C10G73/02 , C10G17/00
CPC分类号： C10G49/002 , C10G67/04 , Y10S203/06
摘要： A hydroprocessing process for removing impurities from a feed comprising a hydrocarbonaceous liquid comprises at least two cocurrent, upflow hydroprocessing reaction stages and a non-catalytic, vapor-liquid contacting stage. The reaction and contacting stages may all be in the same reactor vessel. The feed and a hydrogen treat gas are passed up into a catalyst bed which comprises the first reaction stage, which produces a partially hydroprocessed liquid and vapor effluent. This first stage vapor is passed up into the contacting stage in which it contacts a hydrocarbonaceous liquid which reduces the vapor impurity content. The impurity-enriched contacting liquid passes down and mixes with the first stage liquid effluent. The combined effluents and hydrogen are passed up into the second reaction stage to form a processed product liquid and hydrogen-containing vapor effluent. This second reaction stage vapor effluent is passed up into the first stage to provide at least a portion of the hydrogen for the first stage reaction. Additional product liquid may be recovered by cooling the contacting and condensing the purified contacting stage vapor effluent.
摘要翻译：用于从包含烃液体的进料中除去杂质的加氢处理方法包括至少两个并流，向上加氢处理反应阶段和非催化气液接触阶段。反应和接触阶段都可以在同一反应容器中。进料和氢气处理气体被送入催化剂床，催化剂床包括第一反应段，其产生部分加氢处理的液体和蒸气流出物。该第一级蒸气通入其接触阶段，在该阶段中，其接触含烃液体，这降低了蒸气杂质含量。杂质富集的接触液体向下流动并与第一级液体流出物混合。将合并的废水和氢气输送到第二反应阶段以形成加工产物液体和含氢蒸汽流出物。将该第二反应段蒸气流出物向上流入第一阶段以提供用于第一阶段反应的氢的至少一部分。可以通过冷却接触并冷凝纯化的接触级蒸气流出物来回收附加的产物液体。

86. 发明授权

US5985131A Hydroprocessing in a countercurrent reaction vessel 失效
标题翻译：在逆流反应容器中进行加氢处理
公开(公告)号：US5985131A
公开(公告)日：1999-11-16
申请号：US701925
申请日：1996-08-23
申请人： Ramesh Gupta , David C. Dankworth , Dennis D. Fleming , Edward S. Ellis , James J. Schorfheide
发明人： Ramesh Gupta , David C. Dankworth , Dennis D. Fleming , Edward S. Ellis , James J. Schorfheide
IPC分类号： B01J8/02 , B01J8/04 , B01J29/064 , C10G45/04 , C10G45/44 , C10G47/02 , C10G49/00 , C10G65/00 , C10G65/02 , C10G65/04 , C10G65/08 , C10G65/12 , C10G45/00 , C10G41/00
CPC分类号： B01J8/0278 , B01J29/064 , B01J8/0453 , B01J8/0492 , C10G49/002 , C10G65/02 , C10G65/12
摘要： A process for upgrading a liquid petroleum or chemical stream wherein said stream flows countercurrent to the flow of a treat gas, such as a hydrogen-containing gas, in at least one reaction zone. The reaction vessel used in the practice of the present invention contains vapor and optionally liquid passageway means to bypass one or more catalyst beds. This permits more stable and efficient reaction vessel operation.
摘要翻译：一种用于升级液体石油或化学物流的方法，其中所述流与至少一个反应区中的处理气体（例如含氢气体）的流动逆流流动。在本发明的实践中使用的反应容器包含蒸汽和任选的液体通道装置来绕过一个或多个催化剂床。这允许更稳定和有效的反应容器操作。

87. 发明授权

US5968346A Two stage hydroprocessing with vapor-liquid interstage contacting for vapor heteroatom removal 有权
标题翻译：双级加氢处理，气 - 液间级接触气相除去杂原子
公开(公告)号：US5968346A
公开(公告)日：1999-10-19
申请号：US153921
申请日：1998-09-16
申请人： Henry Jung , Ramesh Gupta , Edward S. Ellis , William E. Lewis
发明人： Henry Jung , Ramesh Gupta , Edward S. Ellis , William E. Lewis
IPC分类号： C10G65/02 , C10G45/02 , C10G65/04 , C10G65/10 , C10G65/12 , C10G70/06
CPC分类号： C10G65/12 , C10G65/04 , C10G65/10 , C10G70/06
摘要： A hydroprocessing process includes two hydroprocessing reaction stages, both of which produce a liquid and a vapor effluent, and a liquid-vapor contacting stage. The first stage vapor effluent contains impurities, such as heteroatom compounds, which are removed from the vapor by contact with processed liquid effluent derived from one or both reaction stages and, optionally, also liquid recovered from processed vapor. The first and contact stage liquid effluents are passed into the second stage to finish the hydoprocessing. The contact and second stage vapor effluents are cooled to recover additional hydroprocessed product liquid.
摘要翻译：加氢处理方法包括两个加氢处理反应阶段，它们都产生液体和蒸汽流出物，以及液 - 气接触阶段。第一级蒸汽流出物含有诸如杂原子化合物的杂质，其通过与来自一个或两个反应级的处理液体流出物接触而从蒸气中除去，并且任选地还含有从经处理的蒸气回收的液体。第一阶段和接触阶段的液体流出物进入第二阶段以完成加氢处理。将接触和第二级蒸汽流出物冷却以回收另外的加氢处理产物液体。

88. 发明授权

US4526757A Pulsed flow vapor-liquid reactor 失效
标题翻译：脉冲流气液反应器
公开(公告)号：US4526757A
公开(公告)日：1985-07-02
申请号：US437905
申请日：1982-11-01
申请人： Ramesh Gupta
发明人： Ramesh Gupta
IPC分类号： B01J8/04 , G05D9/00 , B01J8/02
CPC分类号： B01J8/0492 , Y10S423/09 , Y10T137/2774 , Y10T137/2802
摘要： A process for automatically providing for periodic surge flow or liquid slugs in the catalyst bed to insure that the catalyst is periodically fully wetted. Therefore, before dry spots develop in the bed and some catalyst particles are deprived of the liquid reactants, the aforesaid liquid pulse or slug will rewet the catalyst. This desired periodic introduction of a liquid slug through a catalyst bed is accomplished by the provision of a plurality of automatically actuating and operating siphon means disposed and distributed across the area of the distributor tray means within the reactor.
摘要翻译：一种用于在催化剂床中自动提供周期性浪涌流动或液体段的过程，以确保催化剂周期性地完全润湿。因此，在床上发生干斑之前，一些催化剂颗粒被剥夺了液体反应物，所以前述的液体脉冲或细粒将再润湿催化剂。通过设置多个自动致动和操作的虹吸装置来实现液体塞通过催化剂床的周期性引入，该多个自动启动和操作的虹吸装置设置并分布在反应器内的分配器托盘装置的区域上。

89. 发明授权

US4385033A Reactor for fouling prone feeds 失效
标题翻译：反应堆污染倾向饲料
公开(公告)号：US4385033A
公开(公告)日：1983-05-24
申请号：US336420
申请日：1981-12-31
申请人： Ramesh Gupta
发明人： Ramesh Gupta
IPC分类号： B01J8/02 , B01J8/04 , C10G49/00
CPC分类号： B01J8/0492 , B01J8/0278 , B01J8/0453 , C10G49/002
摘要： The invention is for a fixed bed reactor with two phase gas and liquid flow. The reactor has at least one auxiliary bed of solid particles disposed above the main bed of solid particles. The auxiliary bed has a liquid bypass comprised of hollow tubing extending through the auxiliary bed. Liquid receptacles provide a liquid seal above the liquid bypasses, thereby preventing gas from bypassing along with the liquid. The liquid spilled from the flow receptacles seeks its lowest level and flows through the auxiliary bed. The tubing provides a bypass first for the liquid and later for both the liquid and gas when the auxiliary bed becomes fouled and the liquid seal is thereby broken. This feed arrangement allows for a low pressure drop bypassing of the auxiliary bed, when the auxiliary bed becomes fouled and clogged. The invention is also applicable to other apparatuses which use a flow arrangement similar to fixed bed reactors, but which do not necessarily utilize a chemical reaction. One example of such apparatus is a packed absorption tower having co-current downflow of gas and liquid.
摘要翻译：本发明是用于具有两相气体和液体流的固定床反应器。反应器具有至少一个固体颗粒辅助床，其设置在固体颗粒主床上方。辅助床具有包括延伸穿过辅助床的中空管的液体旁路。液体容器在液体旁路之上提供液体密封，从而防止气体与液体一起旁路。从流动容器溢出的液体寻求其最低水平并流过辅助床。当辅助床被污染并且液体密封件被破坏时，管道首先为液体提供旁路并且随后用于液体和气体。当辅助床被弄脏并堵塞时，该馈送装置允许辅助床的低压降旁路。本发明也适用于使用类似于固定床反应器但不一定利用化学反应的流动布置的其它装置。这种装置的一个实例是具有气流和液体的并流下流的填充吸收塔。

90. 发明授权

US4380529A Hydroprocessing reactor with extended operating life 失效
标题翻译：加氢处理反应器具有延长的使用寿命
公开(公告)号：US4380529A
公开(公告)日：1983-04-19
申请号：US261985
申请日：1981-05-08
申请人： Ramesh Gupta
发明人： Ramesh Gupta
IPC分类号： B01J8/02 , B01J8/04 , C10G49/00 , C10G23/02
CPC分类号： C10G49/002 , B01J8/0278 , B01J8/0453 , B01J8/0492
摘要： The invention is for a fixed bed reactor with two phase gas and liquid flow. The reactor has at least one auxiliary bed of solid particles disposed above the main bed of solid particles. The auxiliary bed has separate liquid and gas bypasses comprised of hollow tubing extending through the auxiliary bed to a distributor tray. A liquid layer on the tray provides a liquid seal above the liquid bypasses, thereby preventing gas from bypassing along with the liquid. This feed arrangement allows for a low pressure drop bypassing of the auxiliary bed, when the auxiliary bed becomes fouled and clogged. The invention is also applicable to other apparatuses which use a flow arrangement similar to fixed bed reactors, but which do not necessarily utilize a chemical reaction. One example of such apparatus is a packed absorption tower having co-current downflow of gas and liquid.
摘要翻译：本发明是用于具有两相气体和液体流的固定床反应器。反应器具有至少一个固体颗粒辅助床，其设置在固体颗粒主床上方。辅助床具有分离的液体和气体旁路，其包括通过辅助床延伸到分配器托盘的中空管。托盘上的液体层在液体旁路上提供液体密封，从而防止气体与液体一起旁路。当辅助床被弄脏并堵塞时，该馈送装置允许辅助床的低压降旁路。本发明也适用于使用类似于固定床反应器但不一定利用化学反应的流动布置的其它装置。这种装置的一个实例是具有气流和液体的并流下流的填充吸收塔。

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