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1. 发明授权

US5876469A Method of heat transfer in reformer 失效
标题翻译：重整器传热方法
公开(公告)号：US5876469A
公开(公告)日：1999-03-02
申请号：US748723
申请日：1996-11-14
申请人： Nobuo Moriya , Takao Kawai , Hiroshi Yagi , Ryosuke Shimizu , Yasumasa Morita
发明人： Nobuo Moriya , Takao Kawai , Hiroshi Yagi , Ryosuke Shimizu , Yasumasa Morita
IPC分类号： B01J8/06 , C01B3/38 , H01M8/06 , C10J1/28 , B01J8/04
CPC分类号： H01M8/0631 , B01J8/067 , C01B3/384 , B01J2208/00212 , C01B2203/0233 , C01B2203/066 , C01B2203/0805 , C01B2203/0811 , C01B2203/0822 , C01B2203/0827 , C01B2203/0833 , C01B2203/0844 , C01B2203/0866 , C01B2203/1041 , C01B2203/1241 , C01B2203/80 , Y02P20/128
摘要： A reformed gas composed mainly of hydrogen and carbon monoxide to be used for a fuel cell is produced by using a multi-tubular reformer provided with bayonet type double-wall catalyst tubes and feeding hydrocarbon gas such as natural gas and steam to the reformer. Porous media of a ceramic material are arranged in such a manner in a shell side flue gas inlet part of the interior of the reformer as to envelop the leading end parts of the catalyst tubes. The transfer of heat from the flue gas to the catalyst tubes is enhanced because the porous media accumulate the heat from the flue gas and radiate the accumulated heat in the direction of the walls of the outer tubes of the catalyst tubes. The otherwise possible uneven transfer of heat to the catalyst tubes is prevented because the wall effect and the channelling of the flue gas are repressed. This invention, therefore, permits effective utilization of the thermal energy of the flue gas for the reforming reaction and enables the reformer to be stably operated.
摘要翻译：通过使用设置有卡口式双壁催化剂管的多管重整器，并将碳氢化合物气体如天然气和蒸汽加入到重整器中，生产主要用于燃料电池的氢和一氧化碳的重整气体。陶瓷材料的多孔介质以这种方式设置在重整器内部的壳侧烟道气入口部分中，以包封催化剂管的前端部分。由于多孔介质积聚来自烟道气的热量并且在催化剂管的外管的壁的方向上辐射累积的热量，所以将热量从烟道气传递到催化剂管被增强。否则可能不均匀地传递热量到催化剂管，因为壁效应和烟气的通道被压制。因此，本发明允许有效利用用于重整反应的烟道气的热能，并使重整器稳定地工作。

2. 发明授权

US08974660B2 Method for upgrading hydrocarbon compounds and a hydrocarbon compound distillation separation apparatus 有权
标题翻译：烃类化合物的改质方法和烃类化合物蒸馏分离装置
公开(公告)号：US08974660B2
公开(公告)日：2015-03-10
申请号：US13138482
申请日：2010-02-26
申请人： Yuichi Tanaka , Yasumasa Morita , Kenichi Kawazuishi
发明人： Yuichi Tanaka , Yasumasa Morita , Kenichi Kawazuishi
IPC分类号： C10G7/00 , C10G45/02 , C10G45/00 , C07C27/06 , C10G2/00
CPC分类号： C10G7/00 , C10G2/32 , C10G53/16 , C10G2300/1022 , C10G2400/02 , C10G2400/06 , C10G2400/08
摘要： There is provided a method for upgrading hydrocarbon compounds, in which hydrocarbon compounds synthesized in a Fisher-Tropsch synthesis reaction are fractionally distillated, and the fractionally distillated hydrocarbon compounds are hydrotreated to produce liquid fuel products. The method includes fractionally distilling heavy hydrocarbon compounds synthesized in the Fisher-Tropsch synthesis reaction as a liquid into a first middle distillate and a wax fraction, and fractionally distilling light hydrocarbon compounds synthesized in the Fisher-Tropsch synthesis reaction as a gas into a second middle distillate and a light gas fraction.
摘要翻译：提供了一种用于升级烃化合物的方法，其中在费 - 托合成反应中合成的烃化合物被分馏，并且分馏馏分的烃化合物被加氢处理以产生液体燃料产物。该方法包括将在费 - 托合成反应中合成的重烃化合物作为液体分馏成第一中间馏分和蜡馏分，并将在费 - 托合成反应中合成的轻质烃化合物分馏为第二中间馏分馏出物和轻质气体馏分。

3. 发明申请

US20090220389A1 BUBBLE COLUMN-TYPE FISCHER-TROPSCH SYNTHESIS SLURRY BED REACTION SYSTEM 有权
标题翻译：泡沫柱型FISCHER-TROPSCH合成浆液反应系统
公开(公告)号：US20090220389A1
公开(公告)日：2009-09-03
申请号：US12097161
申请日：2005-12-14
申请人： Yasuhiro Onishi , Kenichiro Fujimoto , Masaru Ihara , Yoshifumi Suehiro , Yasumasa Morita , Kiyoshi Inaba , Toshio Shimizu , Osamu Iwamoto
发明人： Yasuhiro Onishi , Kenichiro Fujimoto , Masaru Ihara , Yoshifumi Suehiro , Yasumasa Morita , Kiyoshi Inaba , Toshio Shimizu , Osamu Iwamoto
IPC分类号： B01J8/24
CPC分类号： B01J8/228 , B01J8/007 , B01J8/085 , B01J8/1818 , B01J8/22 , B01J2208/00123 , B01J2208/00539 , B01J2208/0061 , C10G2/342 , C10G2300/4006 , C10G2300/805
摘要： A bubble column-type slurry bed reaction system is provided in which an operating system, which synthesizes liquid hydrocarbons by the Fischer-Tropsch (FT) synthesis reaction and separates and derives a catalyst and liquid hydrocarbon products from a slurry composed of gas, liquid and solid phases, can be simplified, and deterioration of catalyst particles caused by attrition and so forth can be reduced. In this FT synthesis reaction system, a bubble column-type slurry bed Fischer-Tropsch synthesis reaction process, in which synthesis gas supplied continuously from the bottom of a reactor and suspended catalyst particles are contacted to form liquid hydrocarbons, gaseous hydrocarbons and water, a process in which a slurry of suspended liquid products formed in the Fischer-Tropsch synthesis reaction process and catalyst particles moves from the reactor to the lower portion of a separation vessel through a downwardly inclined transfer pipe to separate the catalyst particles and gaseous products, a process in which the liquid products formed in the Fischer-Tropsch synthesis reaction process is sent to the separation vessel through a horizontal connecting pipe installed above the downwardly inclined transfer pipe and derived from its apex, a process in which liquid products are derived from the separation vessel, and a process in which aslurry in which catalyst particles are concentrated is derived from the bottom of the separation vessel and circulated to the bottom of the reactor, are driven by the driving force of synthesis gas introduced from the bottom of the reactor and which rises through the slurry bed reactor without using an external drive power source for circulation, and the formed liquid hydrocarbon products, gaseous hydrocarbon products and water are separated and derived without using an external drive power source for separation.
摘要翻译：提供了一种气泡塔型浆床反应系统，其中通过费 - 托（FT）合成反应合成液态烃的操作系统，分离并从由气体，液体和可以简化固相，并且可以减少由磨损等引起的催化剂颗粒的劣化。在该FT合成反应系统中，将泡沫塔型浆料床费 - 托合成反应过程从反应器底部连续供应的合成气和悬浮的催化剂颗粒接触形成液态烃，气态烃和水，其中在费 - 托合成反应过程中形成的悬浮液体产物的浆料和催化剂颗粒通过向下倾斜的转移管从反应器移动到分离容器的下部以分离催化剂颗粒和气态产物的过程，其中在费 - 托合成反应过程中形成的液体产物通过安装在向下倾斜的输送管上方并从其顶点衍生的水平连接管送到分离容器，其中液体产物从分离容器，以及其中催化剂颗粒浓缩的浆料的方法来自分离容器的底部并循环到反应器的底部，由从反应器底部引入并通过浆料床反应器的合成气的驱动力驱动，而不使用外部驱动电源循环，并且形成的液体烃产物，气态烃产物和水分离和衍生而不使用外部驱动电源进行分离。

4. 发明申请

US20110309000A1 METHOD FOR UPGRADING HYDROCARBON COMPOUNDS AND A HYDROCARBON COMPOUND DISTILLATION SEPARATION APPARATUS 有权
标题翻译：升华化合物和烃化合物蒸馏分离装置的方法
公开(公告)号：US20110309000A1
公开(公告)日：2011-12-22
申请号：US13138482
申请日：2010-02-26
申请人： Yuichi Tanaka , Yasumasa Morita , Kenichi Kawazuishi
发明人： Yuichi Tanaka , Yasumasa Morita , Kenichi Kawazuishi
IPC分类号： C10G45/00 , C10G1/02
CPC分类号： C10G7/00 , C10G2/32 , C10G53/16 , C10G2300/1022 , C10G2400/02 , C10G2400/06 , C10G2400/08
摘要： There is provided a method for upgrading hydrocarbon compounds, in which hydrocarbon compounds synthesized in a Fisher-Tropsch synthesis reaction are fractionally distillated, and the fractionally distillated hydrocarbon compounds are hydrotreated to produce liquid fuel products. The method includes fractionally distilling heavy hydrocarbon compounds synthesized in the Fisher-Tropsch synthesis reaction as a liquid into a first middle distillate and a wax fraction, and fractionally distilling light hydrocarbon compounds synthesized in the Fisher-Tropsch synthesis reaction as a gas into a second middle distillate and a light gas fraction.
摘要翻译：提供了一种用于升级烃化合物的方法，其中在费 - 托合成反应中合成的烃化合物被分馏，并且分馏馏分的烃化合物被加氢处理以产生液体燃料产物。该方法包括将在费 - 托合成反应中合成的重烃化合物作为液体分馏成第一中间馏分和蜡馏分，并将在费 - 托合成反应中合成的轻质烃化合物分馏为第二中间馏分馏出物和轻质气体馏分。

5. 发明申请

US20110042619A1 OPERATION METHOD OF SYNTHESIS GAS REFORMER IN GTL PLANT 有权
标题翻译： GTL工厂合成气转化器的运行方法
公开(公告)号：US20110042619A1
公开(公告)日：2011-02-24
申请号：US12736256
申请日：2009-03-30
申请人： Yasumasa Morita , Kenichi Kawazuishi
发明人： Yasumasa Morita , Kenichi Kawazuishi
IPC分类号： C01B3/24
CPC分类号： C01B3/384 , C01B2203/0233 , C01B2203/0238 , C01B2203/0405 , C01B2203/0415 , C01B2203/043 , C01B2203/0475 , C01B2203/0495 , C01B2203/062 , C01B2203/0811 , C01B2203/0827 , C01B2203/0894 , C01B2203/1058 , C01B2203/1258 , C01B2203/148 , C01B2203/1614 , C01B2203/1628 , C01B2203/169 , C01B2203/1695
摘要： An operation method of a synthesis gas reformer of a GTL (gas to liquids) plant is provided with: setting an operation condition of the synthesis gas reformer; determining control target values of a flow rate of the light hydrocarbon gas, the steam, and the CO2, and an amount of heat needed for the synthesis gas reformer; controlling operation load of the synthesis gas reformer; setting a furnace efficiency of the synthesis gas reformer; calculating a combustion load of a burner of the synthesis gas reformer; calculating a lower heating value of the fuel gas based on a composition measurement of the fuel gas of the burner; determining a control target value of the pressure of the fuel gas; calculating a deviation between the control target value of the pressure of the fuel gas and a measured value of the pressure of the fuel gas; and controlling the temperature of the synthesis gas at the outlet of the synthesis gas reformer by adjusting a pressure control valve provided at an inlet of the burner to compensate for the deviation.
摘要翻译：提供了一种GTL（气 - 液）设备的合成气重整器的操作方法，其特征在于：设置合成气重整器的操作条件; 确定轻烃气体，蒸汽和CO 2的流量的控制目标值和合成气重整器所需的热量; 控制合成气重整器的运行负荷; 设定合成气重整炉的炉效; 计算合成气重整器的燃烧器的燃烧负荷; 基于燃烧器的燃料气体的组成测量值计算燃料气体的较低的热值; 确定燃料气体的压力的控制目标值; 计算燃料气体的压力的控制目标值和燃料气体的压力的测量值之间的偏差; 以及通过调节设置在燃烧器入口处的压力控制阀来控制合成气在重整器出口处的温度，以补偿偏差。

6. 发明申请

US20120159669A1 METHOD FOR ALTERING DEPTH OF FLOWER COLOR FOR THE LIGHTER OR DEEPER 审中-公开
标题翻译：用于改变深度或深度的花色深浅的方法
公开(公告)号：US20120159669A1
公开(公告)日：2012-06-21
申请号：US13378895
申请日：2010-06-01
申请人： Shigeru Iida , Yasumasa Morita , Atsushi Hoshino , Yoshikazu Tanaka , Masako Mizutani
发明人： Shigeru Iida , Yasumasa Morita , Atsushi Hoshino , Yoshikazu Tanaka , Masako Mizutani
IPC分类号： A01H3/04 , C12N15/61 , A01H5/00
CPC分类号： C12N15/825
摘要： Disclosed is a novel method for altering the depth of flower color for the lighter or deeper. Specifically disclosed is a method for altering the depth of flower color of a plant for the lighter or deeper by varying the anthocyanin content in petals of the plant, which comprises a step of regulating the expression of type IV chalcone isomerase in the plant.
摘要翻译：公开了一种用于改变较浅或更深的花色深度的新方法。具体公开的是通过改变植物花瓣中的花青素含量来改变植物的较浅或更深的花色深度的方法，其包括调节植物中IV型查耳酮异构酶表达的步骤。

7. 发明授权

US07847302B2 Blue LED with phosphor layer for producing white light and different phosphor in outer lens for reducing color temperature 有权
标题翻译：蓝色LED与荧光层，用于产生白光和外透镜中不同的荧光体，以降低色温
公开(公告)号：US07847302B2
公开(公告)日：2010-12-07
申请号：US11212280
申请日：2005-08-26
申请人： Grigoriy Basin , Paul S. Martin , Robert Scott West , Yasumasa Morita , Tewe Heemstra
发明人： Grigoriy Basin , Paul S. Martin , Robert Scott West , Yasumasa Morita , Tewe Heemstra
IPC分类号： H01L33/00 , H01J1/62
CPC分类号： H01L33/504 , H01L24/97 , H01L2224/97 , H01L2924/01006 , H01L2924/01013 , H01L2924/0102 , H01L2924/01033 , H01L2924/01051 , H01L2924/01058 , H01L2924/01063 , H01L2924/01079 , H01L2924/01082 , H01L2924/12041 , H01L2933/0041 , H01L2224/81
摘要： A technique for forming a white light LED is disclosed. In one embodiment, the LED emits blue light. A first phosphor for producing red, yellow, yellow-green, or green light is formed to conformably coat the LED die. One suitable deposition technique is electrophoretic deposition (EPD). Over the resulting LED structure is deposited another phosphor (to add the remaining color component) in a binder (e.g., silicone) for encapsulating the die. The blue LED light combines with the two phosphor colors to create white light. Since the two different deposition techniques are independent and easily controllable, the resulting white light temperature is highly controllable and the color emission is substantially uniform.
摘要翻译：公开了一种用于形成白光LED的技术。在一个实施例中，LED发射蓝光。形成产生红色，黄色，黄绿色或绿色光的第一荧光体以适形地涂覆LED管芯。一种合适的沉积技术是电泳沉积（EPD）。在所得到的LED结构之外，将另一种荧光体（以将剩余的颜色成分添加）沉积在用于封装模具的粘合剂（例如硅树脂）中。蓝色LED灯与两种荧光粉相结合，产生白光。由于两种不同的沉积技术是独立且易于控制的，所得到的白光温度是高度可控的，并且颜色发射基本上是均匀的。

8. 发明申请

US20050057144A1 Semiconductor light-emitting device 审中-公开
标题翻译：半导体发光装置
公开(公告)号：US20050057144A1
公开(公告)日：2005-03-17
申请号：US10901991
申请日：2004-07-30
申请人： Yasumasa Morita , Hayato Oba , Shigeo Fujisawa , Minoru Tanaka
发明人： Yasumasa Morita , Hayato Oba , Shigeo Fujisawa , Minoru Tanaka
IPC分类号： H01L33/50 , H01L33/54 , H01L33/56 , H01L33/60 , H01L33/62 , H01L33/00
CPC分类号： H01L33/56 , H01L2224/48091 , H01L2224/48247 , H01L2224/48257 , H01L2224/8592 , H01L2924/181 , H01L2933/0091 , H01L2924/00014 , H01L2924/00012
摘要： A semiconductor light-emitting device can serve as a high-brightness light source with less tone variation. A reflective frame having a conical recess can be provided on a substrate. An LED chip can be mounted on the bottom in the reflective frame. A wavelength converter material is preferably filled in the recess to seal the LED chip. The wavelength converter material can include a fluorescent material and a 20-80 wt. % diffuser mixed in an optically transmissive resin.
摘要翻译：半导体发光器件可以用作具有较少色调变化的高亮度光源。具有锥形凹部的反射框架可以设置在基板上。 LED芯片可以安装在反光框架的底部。波长转换器材料优选地填充在凹部中以密封LED芯片。波长转换器材料可以包括荧光材料和20-80wt。％扩散器混合在光学透射树脂中。

9. 发明授权

US08303848B2 Operation method of synthesis gas reformer in GTL plant 有权
标题翻译： GTL工厂合成气重整器的运行方法
公开(公告)号：US08303848B2
公开(公告)日：2012-11-06
申请号：US12736256
申请日：2009-03-30
申请人： Yasumasa Morita , Kenichi Kawazuishi
发明人： Yasumasa Morita , Kenichi Kawazuishi
IPC分类号： C01B3/26 , C01B3/38
CPC分类号： C01B3/384 , C01B2203/0233 , C01B2203/0238 , C01B2203/0405 , C01B2203/0415 , C01B2203/043 , C01B2203/0475 , C01B2203/0495 , C01B2203/062 , C01B2203/0811 , C01B2203/0827 , C01B2203/0894 , C01B2203/1058 , C01B2203/1258 , C01B2203/148 , C01B2203/1614 , C01B2203/1628 , C01B2203/169 , C01B2203/1695
摘要： An operation method of a synthesis gas reformer of a GTL (gas to liquids) plant is provided with: setting an operation condition of the synthesis gas reformer; determining control target values of a flow rate of the light hydrocarbon gas, the steam, and the CO2, and an amount of heat needed for the synthesis gas reformer; controlling operation load of the synthesis gas reformer; setting a furnace efficiency of the synthesis gas reformer; calculating a combustion load of a burner of the synthesis gas reformer; calculating a lower heating value of the fuel gas based on a composition measurement of the fuel gas of the burner; determining a control target value of the pressure of the fuel gas; calculating a deviation between the control target value of the pressure of the fuel gas and a measured value of the pressure of the fuel gas; and controlling the temperature of the synthesis gas at the outlet of the synthesis gas reformer by adjusting a pressure control valve provided at an inlet of the burner to compensate for the deviation.
摘要翻译：提供了一种GTL（气 - 液）设备的合成气重整器的操作方法，其特征在于：设置合成气重整器的操作条件; 确定轻烃气体，蒸汽和CO 2的流量的控制目标值和合成气重整器所需的热量; 控制合成气重整器的运行负荷; 设定合成气重整炉的炉效; 计算合成气重整器的燃烧器的燃烧负荷; 基于燃烧器的燃料气体的组成测量值计算燃料气体的较低的热值; 确定燃料气体的压力的控制目标值; 计算燃料气体的压力的控制目标值和燃料气体的压力的测量值之间的偏差; 以及通过调节设置在燃烧器入口处的压力控制阀来控制合成气在重整器出口处的温度，以补偿偏差。

10. 发明授权

US08057744B2 Bubble column-type Fischer-Tropsch synthesis slurry bed reaction system 有权
标题翻译：泡沫塔型费 - 托合成浆床反应体系
公开(公告)号：US08057744B2
公开(公告)日：2011-11-15
申请号：US12097161
申请日：2005-12-14
申请人： Yasuhiro Onishi , Kenichiro Fujimoto , Masaru Ihara , Yoshifumi Suehiro , Yasumasa Morita , Kiyoshi Inaba , Toshio Shimizu , Osamu Iwamoto
发明人： Yasuhiro Onishi , Kenichiro Fujimoto , Masaru Ihara , Yoshifumi Suehiro , Yasumasa Morita , Kiyoshi Inaba , Toshio Shimizu , Osamu Iwamoto
IPC分类号： B01J8/18 , F27B15/08
CPC分类号： B01J8/228 , B01J8/007 , B01J8/085 , B01J8/1818 , B01J8/22 , B01J2208/00123 , B01J2208/00539 , B01J2208/0061 , C10G2/342 , C10G2300/4006 , C10G2300/805
摘要： According to an exemplary embodiment, a bubble column-type slurry bed Fischer-Tropsch synthesis reaction process can be provided, in which synthesis gas supplied continuously from the bottom of a reactor contacts suspended catalyst particles to form liquid hydrocarbons, gaseous hydrocarbons and water. Additionally, a slurry of suspended liquid products and catalyst particles can move from the reactor to the lower portion of a separation vessel to separate the catalyst particles and gaseous products. Further, a process can be provided in which the liquid products formed are sent to the separation vessel a process in which liquid products can be derived. Additionally, a process can be provided in which a slurry in which catalyst particles are concentrated is derived from the bottom of the separation vessel and circulated to the bottom of the reactor, are driven by the driving force of synthesis gas without using an external drive power source.
摘要翻译：根据示例性实施例，可以提供泡沫塔型浆料床费 - 托合成反应方法，其中从反应器底部连续供应的合成气与悬浮的催化剂颗粒接触以形成液体烃，气态烃和水。此外，悬浮液体产物和催化剂颗粒的浆料可以从反应器移动到分离容器的下部，以分离催化剂颗粒和气态产物。此外，可以提供将所形成的液体产品送到分离容器的方法，其中可以得到液体产物的过程。此外，可以提供一种方法，其中催化剂颗粒浓缩的浆料从分离容器的底部衍生并循环到反应器的底部，由合成气的驱动力驱动，而不使用外部驱动力资源。

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