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11. 发明授权

US07189371B2 Fuel reforming system 有权
标题翻译：燃料重整系统
公开(公告)号：US07189371B2
公开(公告)日：2007-03-13
申请号：US10048023
申请日：2001-05-08
申请人： Yasukazu Iwasaki
发明人： Yasukazu Iwasaki
IPC分类号： B32B5/02 , B32B27/04 , B01J8/00 , C10L3/00
CPC分类号： H01M8/04425 , B01B1/005 , B01J8/001 , B01J19/0006 , B01J2219/00063 , B01J2219/00164 , B01J2219/00198 , B01J2219/00218 , B01J2219/00231 , C01B3/323 , C01B3/48 , C01B3/583 , C01B2203/0244 , C01B2203/0283 , C01B2203/044 , C01B2203/047 , C01B2203/066 , C01B2203/0811 , C01B2203/0822 , C01B2203/0827 , C01B2203/0844 , C01B2203/0866 , C01B2203/1223 , C01B2203/1235 , C01B2203/1276 , C01B2203/1288 , C01B2203/142 , C01B2203/1619 , C01B2203/1633 , C01B2203/1638 , C01B2203/169 , C01B2203/82 , H01M8/04373 , H01M8/04402 , H01M8/0441 , H01M8/04776 , H01M8/04828 , H01M8/04992 , H01M8/0612 , Y02P20/128
摘要： The invention presents a fuel reforming technique for a mobile fuel cell system capable of obtaining a reformed gas composition usable in fuel cell 200 even if vapor temperature supplied from an evaporator 102 into a fuel reformer 107 varies significantly.This system comprises means 601, 602 for detecting the flow rate of fuel vapor and oxygen to be supplied into the fuel reformer 107, and means 600 for detecting at least temperature of fuel vapor to be supplied into the fuel reformer, temperature of oxygen, and temperature of mixed gas of fuel vapor and oxygen, in which the ratio of the flow rate of fuel vapor and the flow rate of oxygen is corrected on the basis of the signal value of the temperature detecting means, and oxygen is supplied depending on the corrected ratio.
摘要翻译：本发明提供一种即使从蒸发器102供给燃料重整器107的蒸气温度显着变化的能够获得可用于燃料电池200的重整气体组成的移动式燃料电池系统的燃料重整技术。该系统包括用于检测燃料蒸气和供应到燃料重整器107中的氧的流量的装置601,602，以及用于检测供应到燃料重整器中的燃料蒸气的至少温度，氧气温度和基于温度检测装置的信号值校正燃料蒸汽和氧气的流量比与燃料蒸汽和氧气的混合气体的温度，根据校正后的氧气供给氧气比。

12. 发明授权

US07163566B2 Method of operating a gas generating system and a gas generating system 失效
标题翻译：操作气体发生系统和气体发生系统的方法
公开(公告)号：US07163566B2
公开(公告)日：2007-01-16
申请号：US09985644
申请日：2001-11-05
申请人： Fabian Döling , Martina Fischer , Uwe Griesmeier , Jochen Nussbaumer
发明人： Fabian Döling , Martina Fischer , Uwe Griesmeier , Jochen Nussbaumer
IPC分类号： C01B3/36
CPC分类号： C01B3/386 , B01J8/0221 , B01J8/0278 , B01J2208/00061 , B01J2208/00628 , B01J2219/00198 , B01J2219/002 , B01J2219/00213 , B01J2219/00218 , B01J2219/00231 , C01B3/382 , C01B2203/142
摘要： A method of operating a gas generating system for generating a hydrogen-rich product gas by partial oxidation or autothermal reforming includes operating a reactor approximately adiabatically. The ratio of the mole flow O2/mole flow C-atomsfuel (O2/C ratio) is controlled on the basis of the temperature of the educts and of the reaction temperature. For adjusting and maintaining an optimal O2/C ratio with respect to a high hydrogen yield, approximately an O2/C ratio corresponding of the present educt temperatures is adjusted and is corrected on the basis of the deviation of the reaction temperature from a desired reaction temperature. The O2/C ratio is then adjusted by controlling the oxygen-containing educt or the hydrocarbon-containing educt.
摘要翻译：操作通过部分氧化或自热重整产生富氢产物气体的气体发生系统的方法包括大致绝热地操作反应器。摩尔流O 2 /摩尔流C原子（O 2 / C / C比）的比例基于离子的温度和反应温度。为了相对于高氢产率调节和保持最佳的O 2 / C比，调节对应于当前流出温度的大约O 2 / C比，并且是基于反应温度与所需反应温度的偏差校正。然后通过控制含氧离子或含烃的析出物来调节O 2 / C比。

13. 发明授权

US07102030B2 Method for managing operation of gas phase reaction apparatus 失效
标题翻译：气相反应装置运行管理方法
公开(公告)号：US07102030B2
公开(公告)日：2006-09-05
申请号：US10796254
申请日：2004-03-09
申请人： Kenji Sanada , Yukihiro Matsumoto , Takeshi Nishimura , Harunori Hirao
发明人： Kenji Sanada , Yukihiro Matsumoto , Takeshi Nishimura , Harunori Hirao
IPC分类号： C07C51/16
CPC分类号： B01J19/002 , B01J8/0453 , B01J8/0492 , B01J23/8885 , B01J2208/00132 , B01J2219/00006 , B01J2219/00164 , B01J2219/00198 , B01J2219/002 , B01J2219/00216 , B01J2219/0022 , B01J2219/00225 , B01J2219/00268 , C07C51/252 , C07C57/04
摘要： A method for managing the operation of an apparatus for the reaction of gas phase partial oxidation of an unsaturated hydrocarbon with a molecular oxygen-containing gas for the purpose of omitting wasteful emergency stop of the operation and ensuring execution of necessary emergency measure and a method for producing (meth) acrylic acid by utilizing the method mentioned above are provided. The operation of the apparatus is brought to emergency stop exclusively when thee values of concentrations of various gases obtained by calculation from the flow rates of the gases being introduced at the inlet port of the reactor and the measured values obtained by analysis with gas analyzing instruments both deviate from the ranges of the present values.
摘要翻译：用于管理不饱和烃与分子氧气体的气相部分氧化反应装置的操作的方法，以省略浪费的紧急停止操作并确保执行必要的应急措施和方法提供了通过利用上述方法生产（甲基）丙烯酸的方法。仅当通过计算得到的各种气体的浓度从在反应器的入口处引入的气体的流量和通过气体分析仪器的分析得到的测量值的值达到紧急停止时，设备的操作才被紧急停止偏离当前值的范围。

14. 发明申请

US20060000748A1 Method for metering catalyst in a fluid catalytic cracking catalyst injection system 有权
公开(公告)号：US20060000748A1
公开(公告)日：2006-01-05
申请号：US11168685
申请日：2005-06-28
申请人： Martin Evans
发明人： Martin Evans
IPC分类号： C10G11/00
CPC分类号： B01J8/0015 , B01J8/18 , B01J2208/00539 , B01J2208/00619 , B01J2208/00752 , B01J2219/00198 , B01J2219/00231 , C10G11/18 , C10G11/187
摘要： A method and apparatus for metering catalyst in a fluid catalytic cracking catalyst injection system are provided. In one embodiment, apparatus for metering catalyst in a fluid catalytic cracking catalyst injection system includes a low pressure storage vessel coupled to a pressure vessel that defines a high pressure side of the apparatus, where the determination of the amount of catalyst transferred is made on the low pressure side of the apparatus.

15. 发明申请

US20050138863A1 Hydrogen refining apparatus 失效
标题翻译：炼氢装置
公开(公告)号：US20050138863A1
公开(公告)日：2005-06-30
申请号：US10980463
申请日：2004-11-03
申请人： Kunihiro Ukai , Kiyoshi Taguchi , Takeshi Tomizawa , Seiji Fujiwara
发明人： Kunihiro Ukai , Kiyoshi Taguchi , Takeshi Tomizawa , Seiji Fujiwara
IPC分类号： B01J8/00 , B01J8/04 , B01J19/00 , B01J19/24 , B01J23/40 , B01J23/63 , C01B3/16 , C01B3/38 , C01B3/48 , C01B3/58 , H01M8/06 , C10K1/00
CPC分类号： B01J19/2485 , B01J8/001 , B01J8/0085 , B01J8/0453 , B01J8/0457 , B01J8/0496 , B01J19/0013 , B01J23/40 , B01J23/63 , B01J2208/00061 , B01J2208/00132 , B01J2208/00168 , B01J2208/00176 , B01J2208/00495 , B01J2208/00504 , B01J2208/0053 , B01J2219/00063 , B01J2219/00081 , B01J2219/00087 , B01J2219/00155 , B01J2219/00157 , B01J2219/00159 , B01J2219/00198 , B01J2219/00202 , C01B3/48 , C01B2203/0233 , C01B2203/0288 , C01B2203/066 , C01B2203/1064 , C01B2203/1076 , C01B2203/1082 , C01B2203/1614 , C01B2203/1619 , C01B2203/1623 , H01M8/0612 , H01M8/0662
摘要： It was difficult to acquire a good CO cleanup efficiency in a hydrogen refining apparatus, for instance, when the start-up and stop operations are frequently repeated. A hydrogen refining apparatus, including a shifter having a shifting catalyst body containing noble metals and metal oxides, and a reforming section for supplying hydrogen gas containing carbon monoxide to the shifter, (1) the temperature of an upstream side of the shifting catalyst body relative to the hydrogen gas flow being substantially between 300° C. and 500° C. and (2) the temperature of a downstream side of the shifting catalyst body relative to the hydrogen gas flow being substantially at 300° C. or less.
摘要翻译：在氢气精炼装置中难以获得良好的CO净化效率，例如，当启动和停止操作经常重复时。一种氢精炼装置，包括具有含有贵金属和金属氧化物的换档催化剂体的换档器和用于向换档器供给含有一氧化碳的氢气的重整部，（1）变换催化剂体相对的上游侧的温度氢气流量基本上在300〜500℃之间，（2）变换催化剂体相对于氢气流的下游侧的温度基本上在300℃以下。

16. 发明授权

US06852307B1 Catalytic oxidation process with flow control system 失效
标题翻译：催化氧化过程与流量控制系统
公开(公告)号：US06852307B1
公开(公告)日：2005-02-08
申请号：US10070213
申请日：2000-08-29
申请人： Herman Pieter Charles Eduard Kuipers , Hendrik Martinus Wentinck
发明人： Herman Pieter Charles Eduard Kuipers , Hendrik Martinus Wentinck
IPC分类号： C01B3/36 , B01J8/02 , B01J12/00 , C01B3/38 , B60K1/00
CPC分类号： C01B3/386 , B01J8/0278 , B01J12/007 , B01J2208/00044 , B01J2208/00061 , B01J2208/00548 , B01J2208/00557 , B01J2208/00628 , B01J2219/00198 , B01J2219/00213 , B01J2219/00231 , C01B2203/0261 , C01B2203/066 , C01B2203/1064 , C01B2203/1205 , C01B2203/1276 , C01B2203/16 , C01B2203/1604 , C01B2203/1619 , C01B2203/169 , C01B2203/84
摘要： A process for the catalytic oxidation of a hydrocarbonaceous fuel into a conversion product, wherein a feed mixture comprising the fuel and an oxygen-containing gas is contacted with a catalyst bed, comprising the steps of: (a) setting the flow rate of the fuel and flow rate of the oxygen-containing gas, (b) determining the actual temperature of the upstream surface of the catalyst bed by mans of a quick response device; and (c) generating an output signal that is a function of the difference between the actual temperature and a set point for the temperature; and using the output signal to adjust the flow rate of the fuel and/or of the oxygen-containing gas.
摘要翻译：一种用于将烃类燃料催化氧化成转化产物的方法，其中包含燃料和含氧气体的进料混合物与催化剂床接触，包括以下步骤：（a）设定燃料的流速和含氧气体的流量，（b）通过快速反应装置确定催化剂床的上游表面的实际温度; 和（c）产生作为温度的实际温度和设定点之差的函数的输出信号; 并且使用输出信号来调节燃料和/或含氧气体的流量。

17. 发明申请

US20040037757A1 Hydrogen purification apparatus 审中-公开
标题翻译：氢气净化装置
公开(公告)号：US20040037757A1
公开(公告)日：2004-02-26
申请号：US10332331
申请日：2003-06-30
发明人： Kiyoshi Taguchi , Kunihiro Ukai , Seiji Fujiwara , Takeshi Tomizawa , Hidenobu Wakita
IPC分类号： B01J008/04
CPC分类号： H01M8/0662 , B01J8/0085 , B01J8/009 , B01J8/048 , B01J8/0496 , B01J19/2485 , B01J23/40 , B01J23/8926 , B01J35/0006 , B01J35/04 , B01J37/0246 , B01J2208/00061 , B01J2219/00198 , B01J2219/002 , B01J2219/00234 , C01B3/583 , C01B2203/044 , C01B2203/047 , C01B2203/066 , H01M8/0668
摘要： A clarifying catalyst body in an apparatus of hydrogen purification is such that a first catalyst containing at least one kind selected from the group consisting of Pt, Pd, Ru and Rh and a second catalyst containing at least one kind selected from the group consisting of Pd, Ru, Rh and Ni are mixed or integrated, The purifying catalyst body in the apparatus of hydrogen purification consists of (1) an oxide containing at least either Al or Si, (2) at least one kind of transition metal and/or a transition metal oxide and (3) at least one kind of noble metal and/or noble metal oxide selected from the group consisting of Pt, Ru, Pd and Rh.
摘要翻译：在氢气净化装置中的澄清催化剂体是使含有选自Pt，Pd，Ru和Rh中的至少一种的第一催化剂和含有选自Pd ，Ru，Rh和Ni混合或整合。氢纯化装置中的净化催化剂体由（1）至少含有Al或Si的氧化物，（2）至少一种过渡金属和/或过渡金属氧化物和（3）选自Pt，Ru，Pd和Rh中的至少一种贵金属和/或贵金属氧化物。

18. 发明申请

US20020056229A1 Method of operating a gas generating system and a gas generating system 失效
标题翻译：操作气体发生系统和气体发生系统的方法
公开(公告)号：US20020056229A1
公开(公告)日：2002-05-16
申请号：US09985644
申请日：2001-11-05
发明人： Fabian Doling , Martina Fischer , Uwe Griesmeier , Jochen Nussbaumer
IPC分类号： C10J001/00 , C10J001/28
CPC分类号： C01B3/386 , B01J8/0221 , B01J8/0278 , B01J2208/00061 , B01J2208/00628 , B01J2219/00198 , B01J2219/002 , B01J2219/00213 , B01J2219/00218 , B01J2219/00231 , C01B3/382 , C01B2203/142
摘要： A method of operating a gas generating system for generating a hydrogen-rich product gas by partial oxidation or autothermal reforming includes operating a reactor approximately adiabatically. The ratio of the mole flow O2/mole flow C-atomsfuel (O2/C ratio) is controlled on the basis of the temperature of the educts and of the reaction temperature. For adjusting and maintaining an optimal O2/C ratio with respect to a high hydrogen yield, approximately an O2/C ratio corresponding of the present educt temperatures is adjusted and is corrected on the basis of the deviation of the reaction temperature from a desired reaction temperature. The O2/C ratio is then adjusted by controlling the oxygen-containing educt or the hydrocarbon-containing educt.
摘要翻译：操作通过部分氧化或自热重整产生富氢产物气体的气体发生系统的方法包括大致绝热地操作反应器。基于蒸馏出的温度和反应温度来控制摩尔流量O 2 /摩尔流量C原子燃料（O 2 / C比）的比率。为了调节和维持相对于高氢产率的最佳O 2 / C比，调节对应于当前流出温度的大致O 2 / C比，并且基于反应温度与所需反应温度的偏差来校正。然后通过控制含氧离子或含烃的离子发生器来调节O 2 / C比。

19. 发明授权

US06174927B1 Exothermic catalytic chemical process 失效
标题翻译：放热催化化学工艺
公开(公告)号：US06174927B1
公开(公告)日：2001-01-16
申请号：US09142092
申请日：1999-04-06
申请人： Peter Edward James Abbott
发明人： Peter Edward James Abbott
IPC分类号： C07C2700
CPC分类号： B01J8/0285 , B01J8/001 , B01J2208/00044 , B01J2208/00132 , B01J2219/00198 , B01J2219/00202 , B01J2219/00213 , B01J2219/00238 , C07C29/1512 , C07C29/154 , C07C31/04
摘要： An exothermic catalytic process, particularly methanol synthesis, wherein reactants are passed through a fixed bed of a catalyst and heat evolved by the reaction is transferred to at least part of the reactants fed to the catalyst bed by heat exchange means to which said part of the reactants are fed, characterized by operation of the process under conditions whereby increasing the temperature at which said reactants are fed to the catalyst bed has the effect of increasing the temperature to which said reactants are heated in said heat exchange means, and vice versa, and controlling said process by monitoring the temperature of said reactants leaving said heat exchange means and/or entering said bed, decreasing the temperature at which the reactants are fed to said heat exchange means in response to any increase in said monitored temperature from a desired level, and increasing the temperature at which the reactants are fed to said heat exchange means in response to any decrease in said monitored temperature from said desired level.
摘要翻译：放热催化方法，特别是甲醇合成，其中反应物通过催化剂的固定床和通过反应放出的热量被转移到通过热交换装置供给到催化剂床的反应物的至少一部分，反应物进料，其特征在于在使所述反应物进料到催化剂床的温度升高的条件下操作该方法具有增加所述反应物在所述热交换装置中被加热的温度的作用，反之亦然，以及通过监测离开所述热交换装置和/或进入所述床的所述反应物的温度来控制所述方法，降低反应物响应于所述监测温度从期望水平的任何增加而被供给到所述热交换装置的温度，并且响应于sai的任何减少而增加反应物被供给到所述热交换装置的温度从所述期望的水平监测温度。

20. 发明授权

US5955033A Rotary kiln arrangements 失效
标题翻译：旋转窑装置
公开(公告)号：US5955033A
公开(公告)日：1999-09-21
申请号：US445451
申请日：1993-09-15
申请人： Michael Richard Hayes
发明人： Michael Richard Hayes
IPC分类号： B01J19/00 , B01J19/28 , C01G43/025 , F27B7/10 , F27B7/20 , F27B7/32 , F27B7/34 , F27B7/42 , F27D21/00 , B01J10/00
CPC分类号： B01J19/0013 , B01J19/28 , C01G43/025 , F27B7/10 , F27B7/20 , F27B7/42 , B01J2219/00051 , B01J2219/00058 , B01J2219/00135 , B01J2219/00198 , B01J2219/002 , B01J2219/0022 , B01J2219/00231 , B01J2219/187 , F27B2007/3217 , F27D21/0014
摘要： A rotary kiln in which reaction is to occur between counterflowing reactants and an injector for a reactant extends into a reaction zone in the kiln. The injector is provided with means for adjusting the temperature of the injected reactant to a temperature in the desired range for that zone. Further means are provided for maintaining a temperature in the desired range throughout the zone. The arrangement be used in the production of uranium oxides from uranium hexafluoride.
摘要翻译：在反向反应物和反应物注射器之间发生反应的回转窑延伸到窑内的反应区。注射器设置有用于将注入的反应物的温度调节到该区域的期望范围内的温度的装置。提供了进一步的装置，用于将温度保持在整个区域的期望范围内。该装置用于从六氟化铀生产铀氧化物。

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