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1. 发明申请

US20120297822A1 SEPARATION OF GASES 有权
标题翻译：气体分离
公开(公告)号：US20120297822A1
公开(公告)日：2012-11-29
申请号：US13575968
申请日：2011-01-21
申请人： Michael Edward Bailey , Stefano Consonni , Jonathan Alec Forsyth , Manuele Gatti , Emanuele Martelli , Yasushi Mori , Kazumasa Ogura , Federico Vigano
发明人： Michael Edward Bailey , Stefano Consonni , Jonathan Alec Forsyth , Manuele Gatti , Emanuele Martelli , Yasushi Mori , Kazumasa Ogura , Federico Vigano
IPC分类号： F25J1/00
CPC分类号： C01B3/506 , C01B3/52 , C01B2203/0415 , C01B2203/046 , C01B2203/0475 , C01B2203/0485 , C01B2203/0805 , C01B2203/0883 , C01B2203/146 , F25J3/0625 , F25J3/0655 , F25J3/067 , F25J2205/40 , F25J2205/50 , F25J2215/04 , F25J2230/30 , F25J2240/30 , F25J2270/06 , Y02C10/12 , Y02P20/152
摘要： A process for separating sour shifted synthesis gas feedstock into liquid carbon dioxide, a gaseous hydrogen-containing gas and separated sulphur-containing components includes the steps of a. scrubbing the sour shifted gas elevated pressure with an alcohol solvent in a first scrubber and separately recovering an alcohol stream containing the sulphur-containing components and a sweet shifted gas; b. thereafter cooling the sweet shifted gas to a temperature and elevated pressure at which the carbon dioxide contained therein condenses and a two-phase gas- liquid mixture is formed; c. separating the two-phase mixture of stage (b) into separate liquid carbon dioxide and gaseous hydrogen-containing fractions in a fractionation unit; d. extracting residual carbon dioxide from the separated gaseous hydrogen-containing fraction by scrubbing the gaseous hydrogen-containing fraction at elevated pressure with an alcohol solvent in a second scrubber and recovering an alcohol stream containing carbon dioxide; e. feeding the alcohol stream containing carbon dioxide produced in step (d) to the first scrubber and f. warming and expanding the scrubber gaseous hydrogen-containing fraction using at least one heat exchanger to exchange heat with the mixture of step (b) and at least one turbo-expander capable of recovering mechanical work. The process described may be used in for example Integrated Gasification Combined Cycles (IGCC) where the source of fuel is coal or low grade carbon sources such as lignite, tar sands and shale oil.
摘要翻译：用于将酸移位的合成气原料分离成液态二氧化碳，含气态气体和分离的含硫组分的方法包括以下步骤：a。在第一洗涤器中用醇溶剂洗涤酸转移气体升高的压力，并单独回收含有含硫成分和甜味转换气体的醇流; b。然后将甜味转移气体冷却至其中所含的二氧化碳冷凝的温度和升高的压力，并形成两相气液混合物; C。将分段（b）的两相混合物分离成分离液体二氧化碳和气态含氢馏分; d。通过在第二洗涤器中用醇溶剂在升高的压力下洗涤含气态气体馏分并回收含二氧化碳的醇流，从分离的含气态氢气馏分中提取残余二氧化碳; e。将步骤（d）中产生的含有二氧化碳的醇流送入第一洗涤器，f。使用至少一个热交换器使洗涤器气态含氢馏分升温和膨胀，以与步骤（b）的混合物和能够回收机械功的至少一个涡轮膨胀机交换热量。所描述的方法可用于例如集成气化组合循环（IGCC），其中燃料源为煤或低等级碳源，例如褐煤，焦油砂和页岩油。

2. 发明授权

US6077140A Screen manufacturing method using flat display panels and radiation mechanism of flat display panels 失效
标题翻译：使用平板显示面板的屏幕制造方法和平板显示面板的辐射机构
公开(公告)号：US6077140A
公开(公告)日：2000-06-20
申请号：US263629
申请日：1999-03-05
申请人： Kazuo Kimura , Kazuhisa Hemmi , Kazumasa Ogura
发明人： Kazuo Kimura , Kazuhisa Hemmi , Kazumasa Ogura
IPC分类号： G09F9/00 , G09F9/313 , G09F9/40 , H01J17/28 , H05K7/20 , H01J9/24
CPC分类号： G09F9/313 , H05K7/20963 , H05K7/20972 , H01J2217/492
摘要： In this screen manufacturing method, a method of effectively cooling flat display panels (1) which form a display screen is provided. A mechanism for cooling the flat display panels (1) is also provided. More specifically, in this manufacturing method, when a display screen (50) is assembled, clearances (41) are provided between modules (40) in which the flat display panels (1) are lined up to, thereby facilitate air circulation driven by a fan (42). Further, a radiation member is fitted to a holder which fixes the flat display panels (1). Thus, a surface area of the holder becomes larger by a portion equivalent to the radiation member, whereby radiative cooling is enhanced.
摘要翻译：在该屏幕制造方法中，提供了有效地冷却形成显示屏的平板显示面板（1）的方法。还提供了用于冷却平板显示面板（1）的机构。更具体地说，在该制造方法中，当组装显示画面（50）时，在平面显示面板（1）排列成的模块（40）之间设置间隙（41），由此便于由风扇（42）。此外，辐射构件装配到固定平面显示面板（1）的保持器。因此，通过与放射部件相当的部分，保持架的表面积变大，由此辐射冷却增强。

3. 发明授权

US4651057A Standing-wave accelerator 失效
标题翻译：驻波加速器
公开(公告)号：US4651057A
公开(公告)日：1987-03-17
申请号：US699441
申请日：1985-02-07
申请人： Isamu Uetomi , Masakazu Kimura , Kazumasa Ogura
发明人： Isamu Uetomi , Masakazu Kimura , Kazumasa Ogura
IPC分类号： H01J25/10 , H01J23/24 , H01P7/06 , H05H9/00 , H05H9/04
CPC分类号： H01J23/24 , H05H9/04
摘要： A standing-wave accelerator including a plurality of accelerating cavities arranged along the axis direction of the accelerator; a plurality of coupling cavities provided between the two-adjacent accelerating cavities; at least one of the coupling cavities is provided with a detuning device for detuning the coupling cavity; and the detuning device is provided to be inserted from a first wall of the coupling cavity to extend until it comes into contact with a second wall thereof, spacedly passed between a pair of inwardly projecting posts.
摘要翻译：一种驻波加速器，包括沿着所述加速器的轴线方向配置的多个加速腔; 设置在所述两个相邻的加速腔之间的多个联接腔; 耦合腔中的至少一个设置有用于使耦合腔失谐的失谐装置; 并且所述失谐装置设置成从所述联接腔的第一壁插入，以延伸直到其与第二壁接触，间隔地通过一对向内突出的柱之间。

4. 发明申请

US20060000355A1 Apparatus for generating freshwater 审中-公开
标题翻译：用于产生淡水的设备
公开(公告)号：US20060000355A1
公开(公告)日：2006-01-05
申请号：US11148451
申请日：2005-06-09
申请人： Kazumasa Ogura , Masaki Iijima
发明人： Kazumasa Ogura , Masaki Iijima
IPC分类号： B01D47/06
CPC分类号： C02F1/16 , B01D1/14 , B01D1/16 , B01D5/003 , C02F1/12 , C02F1/265 , C02F2103/08 , Y02A20/128
摘要： An apparatus for generating freshwater using exhaust combustion gas and seawater includes a water spraying unit that sprays the seawater into the exhaust combustion gas; and a freshwater collecting unit that collects the freshwater from the exhaust combustion gas into which the seawater is sprayed.
摘要翻译：使用排气燃烧气体和海水产生淡水的设备包括：将所述海水喷射到排气燃烧气体中的喷水单元; 以及从被喷射到其中的废气燃烧气体收集淡水的淡水收集单元。

5. 发明授权

US09212061B2 Separation of gases 有权
标题翻译：气体分离
公开(公告)号：US09212061B2
公开(公告)日：2015-12-15
申请号：US13575968
申请日：2011-01-21
申请人： Michael Edward Bailey , Stefano Consonni , Jonathan Alec Forsyth , Manuele Gatti , Emanuele Martelli , Yasushi Mori , Kazumasa Ogura , Federico Vigano
发明人： Michael Edward Bailey , Stefano Consonni , Jonathan Alec Forsyth , Manuele Gatti , Emanuele Martelli , Yasushi Mori , Kazumasa Ogura , Federico Vigano
IPC分类号： F25J3/00 , C01B3/50 , C01B3/52 , F25J3/06
CPC分类号： C01B3/506 , C01B3/52 , C01B2203/0415 , C01B2203/046 , C01B2203/0475 , C01B2203/0485 , C01B2203/0805 , C01B2203/0883 , C01B2203/146 , F25J3/0625 , F25J3/0655 , F25J3/067 , F25J2205/40 , F25J2205/50 , F25J2215/04 , F25J2230/30 , F25J2240/30 , F25J2270/06 , Y02C10/12 , Y02P20/152
摘要： A process for separating sour shifted synthesis gas feedstock into liquid carbon dioxide, a gaseous hydrogen-containing gas and separated sulphur-containing components includes the steps of a. scrubbing the sour shifted gas elevated pressure with an alcohol solvent in a first scrubber and separately recovering an alcohol stream containing the sulphur-containing components and a sweet shifted gas; b. thereafter cooling the sweet shifted gas to a temperature and elevated pressure at which the carbon dioxide contained therein condenses and a two-phase gas-liquid mixture is formed; c. separating the two-phase mixture of stage (b) into separate liquid carbon dioxide and gaseous hydrogen-containing fractions in a fractionation unit; d. extracting residual carbon dioxide from the separated gaseous hydrogen-containing fraction by scrubbing the gaseous hydrogen-containing fraction at elevated pressure with an alcohol solvent in a second scrubber and recovering an alcohol stream containing carbon dioxide; e. feeding the alcohol stream containing carbon dioxide produced in step (d) to the first scrubber and f. warming and expanding the scrubber gaseous hydrogen-containing fraction using at least one heat exchanger to exchange heat with the mixture of step (b) and at least one turbo-expander capable of recovering mechanical work. The process described may be used in for example Integrated Gasification Combined Cycles (IGCC) where the source of fuel is coal or low grade carbon sources such as lignite, tar sands and shale oil.
摘要翻译：用于将酸移位的合成气原料分离成液态二氧化碳，含气态气体和分离的含硫组分的方法包括以下步骤：a。在第一洗涤器中用醇溶剂洗涤酸转移气体升高的压力，并单独回收含有含硫成分和甜味转换气体的醇流; b。然后将甜味转移气体冷却至其中所含的二氧化碳冷凝的温度和升高的压力，并形成两相气液混合物; C。将分段（b）的两相混合物分离成分离液体二氧化碳和气态含氢馏分; d。通过在第二洗涤器中用醇溶剂在升高的压力下洗涤含气态气体馏分并回收含二氧化碳的醇流，从分离的含气态氢气馏分中提取残余二氧化碳; e。将步骤（d）中产生的含有二氧化碳的醇流送入第一洗涤器，f。使用至少一个热交换器使洗涤器气态含氢馏分升温和膨胀，以与步骤（b）的混合物和能够回收机械功的至少一个涡轮膨胀机交换热量。所描述的方法可用于例如集成气化组合循环（IGCC），其中燃料源为煤或低等级碳源，例如褐煤，焦油砂和页岩油。

6. 发明申请

US20120118010A1 SEPARATION OF CARBON DIOXIDE AND HYDROGEN 有权
标题翻译：二氧化碳和氢气的分离
公开(公告)号：US20120118010A1
公开(公告)日：2012-05-17
申请号：US13386692
申请日：2010-07-23
申请人： Jonathan Alec Forsyth , Yasushi Mori , Kazumasa Ogura
发明人： Jonathan Alec Forsyth , Yasushi Mori , Kazumasa Ogura
IPC分类号： F25J3/08
CPC分类号： C10K1/005 , B01D53/002 , B01D53/1462 , B01D53/1468 , B01D2257/304 , B01D2257/504 , C01B3/16 , C01B3/34 , C01B3/506 , C01B3/52 , C01B17/167 , C01B2203/0283 , C01B2203/0415 , C01B2203/046 , C01B2203/0475 , C01B2203/0485 , C01B2203/0495 , C01B2203/0883 , C01B2203/0894 , C01B2203/84 , C10K1/004 , C10K1/165 , F25J3/0625 , F25J3/0655 , F25J3/067 , F25J3/0675 , F25J2205/40 , F25J2205/50 , F25J2210/04 , F25J2220/82 , F25J2220/84 , F25J2230/30 , F25J2245/02 , F25J2270/06 , F25J2270/20 , Y02C10/06 , Y02C10/12 , Y02P20/152
摘要： A process is described for separating a gas stream containing hydrogen sulfide (H2S) impurities into a hydrogen (H2) rich vapour stream, a carbon dioxide (CO2) stream and an H2S rich vapour stream in an apparatus that comprises a compression and/or cooling system comprising at least one compressor and/or heat exchanger and a gas-liquid separator vessel, and an H2S recovery unit. In examples, the process comprises the steps of: (a) feeding the gas stream to the compression and/or cooling system such that carbon dioxide in the gas stream condenses to form a two-phase stream; (b) passing the two-phase stream either directly or indirectly to a gas-liquid separator vessel and withdrawing a hydrogen rich vapour stream and a liquid CO2 stream containing dissolved H2S impurities from the separator vessel; (c) passing the liquid CO2 stream containing dissolved H2S impurities to an H2S recovery unit comprising an evaporator/condenser in which the CO2 and H2S are vaporised and an H2S absorber in which the gaseous H2S and CO2 are separated, wherein the two phase stream passed to the separator is at a pressure of from 80 bar to 400 bar. In some applications, the pressure of the H2S recovery unit is at least 30 bar. In a preferred example, residual CO2 in the hydrogen rich vapour stream is removed in an optional step by solvent extraction in a CO2 absorber most preferably in a configuration where the H2S and CO2 absorbers share the same (preferably methanol) solvent.
摘要翻译：描述了一种方法，用于在包含压缩和/或冷却的装置中将含有硫化氢（H 2 S）杂质的气流分离成富氢的（H 2）蒸气流，二氧化碳（CO 2）流和富H 2 S蒸气流系统，其包括至少一个压缩机和/或热交换器以及气液分离器容器和H 2 S回收单元。在实例中，该方法包括以下步骤：（a）将气流送入压缩和/或冷却系统，使气流中的二氧化碳冷凝形成两相流; （b）将两相流直接或间接地通入气液分离器容器，并从分离器容器中取出富含氢的蒸气流和含有溶解的H 2 S杂质的液体CO 2流; （c）将含有溶解的H 2 S杂质的液体CO 2物流通入包含蒸发器/冷凝器的H 2 S回收单元，其中CO 2和H 2 S被蒸发，其中H2S和CO 2被分离的H2S吸收器，其中两相流通过分离器的压力为80巴至400巴。在一些应用中，H2S回收单元的压力至少为30巴。在优选的实施例中，通过在CO 2吸收剂中最优选以其中H 2 S和CO 2吸收剂共享相同（优选甲醇）溶剂的构型溶剂萃取，在任选的步骤中除去富氢蒸汽流中的残余CO 2。

7. 发明授权

US07544337B2 Impurity disposal system and method 有权
标题翻译：杂质处置系统及方法
公开(公告)号：US07544337B2
公开(公告)日：2009-06-09
申请号：US10563010
申请日：2005-04-08
申请人： Kazumasa Ogura , Masaki Iijima
发明人： Kazumasa Ogura , Masaki Iijima
IPC分类号： B01D53/52 , B01D53/62 , C10G31/00 , C10L3/10
CPC分类号： C10L3/10 , B01D53/1418 , B01D53/1462 , B01D2257/304 , B01D2257/504 , B01D2257/80 , Y02C10/06
摘要： An impurity removing unit removes an impurity gas from a target gas while the target gas is in a gaseous state. A compressing unit compresses the impurity gas to produce compressed impurity gas. A drying unit removes water from the compressed impurity gas to produce a dried compressed impurity gas. A disposing unit disposes the dried compressed impurity gas into an underground aquifer.
摘要翻译：当目标气体处于气态时，杂质去除单元从目标气体中除去杂质气体。压缩单元压缩杂质气体以产生压缩的杂质气体。干燥单元从压缩的杂质气体中除去水以产生干燥的压缩杂质气体。处置单元将干燥的压缩杂质气体置于地下含水层中。

8. 发明授权

US07451604B2 Device and method for vaporizing LNG 有权
标题翻译： LNG蒸发装置及方法
公开(公告)号：US07451604B2
公开(公告)日：2008-11-18
申请号：US10554746
申请日：2005-03-08
申请人： Keijiro Yoshida , Kazumasa Ogura
发明人： Keijiro Yoshida , Kazumasa Ogura
IPC分类号： F17C9/02
CPC分类号： F17C9/02 , F17C2221/033 , F17C2223/0161 , F17C2223/033 , F17C2225/0123 , F17C2225/033 , F17C2225/035 , F17C2225/036 , F17C2227/0313 , F17C2227/0318 , F17C2227/0393 , F17C2227/0395 , F17C2265/05 , F17C2270/0105 , F17C2270/0113 , F17C2270/0121 , F17C2270/0126 , F28D3/00
摘要： An LNG gasifier configured to be installed on an offshore structure for vaporizing LNG includes a water passage into which water flows; an LNG passage provided inside the water passage and configured to pass the LNG and that allows heat exchange between the water and the LNG; and a bubble generating unit configured to generate bubbles of air into the water in the water passage. The water passage has an inlet port from where the water is taken in and a discharge port from where air and the water are discharged.
摘要翻译：构造成安装在用于蒸发LNG的海上结构上的LNG气化器包括水流过水流; LNG通道，其设置在水通道内并且被配置为通过LNG并且允许水和LNG之间的热交换; 以及气泡发生单元，其构造成在水通道中的水中产生空气。水通道具有从其中进入的入口和从空气和水排出的排出口。

9. 发明授权

US07250606B2 Buried object evaluating method, underground resources evaluating method, underground waste evaluating method, underground preserved object evaluating method, stratum structure evaluating method and building interior monitoring method, all using hard X-rays or γ-rays 有权
标题翻译：埋藏物评价方法，地下资源评价方法，地下废物评价方法，地下保护物评价方法，地层结构评价方法和建筑物内部监测方法，均采用硬X射线或γ射线
公开(公告)号：US07250606B2
公开(公告)日：2007-07-31
申请号：US10946080
申请日：2004-09-22
申请人： Kazumasa Ogura , Masaki Iijima , Yoshikatsu Kuroda
发明人： Kazumasa Ogura , Masaki Iijima , Yoshikatsu Kuroda
IPC分类号： G01F23/00 , G01V5/00 , G01V5/08 , G01V5/10 , G01N23/04
CPC分类号： G01V5/02 , G01N23/046 , G01N2223/419 , G01N2223/612 , G01T7/00 , G01V5/0069 , G01V5/06 , G01V5/08
摘要： As a method for using a hard X-ray sensor that can detect weak hard X-rays or the like with a higher resolution, a method for accurately evaluating natural resources of crude oil, natural gas, etc. existing underground, for example, is provided. A buried object evaluating method includes a detecting step of arranging a radiation detector to be opposed to a hard X-ray source radiating first hard X-rays with a buried object buried in a first substance being interposed between the radiation detector and the radiation source and, by using the radiation detector, detecting second hard X-rays transmitted through the buried object out of the first hard X-rays and third hard X-rays not transmitted through the buried object, and an evaluating step of evaluating the buried object based on a strength of the first hard X-rays and a strength of the second hard X-rays detected by the radiation detector.
摘要翻译：作为使用能够以更高分辨率检测弱硬X射线等的硬X射线传感器的方法，例如，准确评价地下现有的原油，天然气等的自然资源的方法是提供。掩埋物体评估方法包括：检测步骤，将放射第一硬X射线的硬X射线源与被埋置在放射线检测器和辐射源之间的第一物质的掩埋物体相对的放射线检测器配置;以及通过使用所述放射线检测器，从不穿过所述被埋物体的第一硬X射线和第三硬X射线检测通过所述掩埋对象物透射的第二硬X射线，以及评价步骤，基于第一硬X射线的强度和由辐射检测器检测到的第二硬X射线的强度。

10. 发明授权

US09163188B2 Separation of carbon dioxide and hydrogen 有权
标题翻译：分离二氧化碳和氢气
公开(公告)号：US09163188B2
公开(公告)日：2015-10-20
申请号：US13386692
申请日：2010-07-23
申请人： Jonathan Alec Forsyth , Yasushi Mori , Kazumasa Ogura
发明人： Jonathan Alec Forsyth , Yasushi Mori , Kazumasa Ogura
IPC分类号： C10K1/00 , B01D53/00 , C01B3/16 , C01B3/34 , C01B3/50 , C01B3/52 , C01B17/16 , C10K1/16 , F25J3/06 , B01D53/14
CPC分类号： C10K1/005 , B01D53/002 , B01D53/1462 , B01D53/1468 , B01D2257/304 , B01D2257/504 , C01B3/16 , C01B3/34 , C01B3/506 , C01B3/52 , C01B17/167 , C01B2203/0283 , C01B2203/0415 , C01B2203/046 , C01B2203/0475 , C01B2203/0485 , C01B2203/0495 , C01B2203/0883 , C01B2203/0894 , C01B2203/84 , C10K1/004 , C10K1/165 , F25J3/0625 , F25J3/0655 , F25J3/067 , F25J3/0675 , F25J2205/40 , F25J2205/50 , F25J2210/04 , F25J2220/82 , F25J2220/84 , F25J2230/30 , F25J2245/02 , F25J2270/06 , F25J2270/20 , Y02C10/06 , Y02C10/12 , Y02P20/152
摘要： A process is described for separating a gas stream containing hydrogen sulfide (H2S) impurities into a hydrogen (H2) rich vapor stream, a carbon dioxide (CO2) stream and an H2S rich vapor stream in an apparatus that comprises a compression and/or cooling system comprising at least one compressor and/or heat exchanger and a gas-liquid separator vessel, and an H2S recovery unit. In examples, the process comprises the steps of: (a) feeding the gas stream to the compression and/or cooling system such that carbon dioxide in the gas stream condenses to form a two-phase stream; (b) passing the two-phase stream either directly or indirectly to a gas-liquid separator vessel and withdrawing a hydrogen rich vapor stream and a liquid CO2 stream containing dissolved H2S impurities from the separator vessel; (c) passing the liquid CO2 stream containing dissolved H2S impurities to an H2S recovery unit comprising an evaporator/condenser in which the CO2 and H2S are vaporized and an H2S absorber in which the gaseous H2S and CO2 are separated, wherein the two phase stream passed to the separator is at a pressure of from 80 bar to 400 bar. In some applications, the pressure of the H2S recovery unit is at least 30 bar. In a preferred example, residual CO2 in the hydrogen rich vapor stream is removed in an optional step by solvent extraction in a CO2 absorber most preferably in a configuration where the H2S and CO2 absorbers share the same (preferably methanol) solvent.
摘要翻译：描述了一种方法，用于在包含压缩和/或冷却的装置中将含有硫化氢（H 2 S）杂质的气流分离成富氢的（H 2）蒸气流，二氧化碳（CO 2）流和富H 2 S蒸气流系统，其包括至少一个压缩机和/或热交换器以及气液分离器容器和H 2 S回收单元。在实例中，该方法包括以下步骤：（a）将气流送入压缩和/或冷却系统，使气流中的二氧化碳冷凝形成两相流; （b）将两相流直接或间接地通入气液分离器容器，并从分离器容器中取出富含氢的蒸气流和含有溶解的H 2 S杂质的液体CO 2流; （c）将含有溶解的H 2 S杂质的液体CO 2物流通入包含蒸发器/冷凝器的H2S回收单元，其中CO 2和H 2 S被蒸发，其中H2S和CO2分离出的H2S吸收器，其中两相流通过分离器的压力为80巴至400巴。在一些应用中，H2S回收单元的压力至少为30巴。在优选的实施例中，通过在CO 2吸收剂中最优选以其中H 2 S和CO 2吸收剂共享相同（优选甲醇）溶剂的构型溶剂萃取，在任选的步骤中除去富氢蒸汽流中的残余CO 2。

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