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公开(公告)号:US20110139047A1
公开(公告)日:2011-06-16
申请号:US13058853
申请日:2009-08-28
申请人: Soken Takase , Katsuhiro Ota , Takao Hashimoto , Takashi Fujii
发明人: Soken Takase , Katsuhiro Ota , Takao Hashimoto , Takashi Fujii
IPC分类号: F23K1/00
CPC分类号: F02C6/10 , C10J3/48 , C10J2200/15 , C10J2300/0909 , C10J2300/093 , C10J2300/0956 , C10J2300/0959 , C10J2300/0969 , C10J2300/1653 , C10J2300/1678 , C10J2300/1815 , F01K23/067 , F02C3/28 , F05D2220/722 , F05D2260/61 , Y02E20/16 , Y02E20/18 , Y02E20/326
摘要: Provided is an air-blown integrated coal gasification combined cycle power generation system equipped with a carbon-dioxide capturing device, in which the integrated coal gasification combined cycle power generation system eliminates the need for an air separator by obtaining a new carrier source that replaces nitrogen gas serving as a carrier gas for pressurizing and carrying pulverized coal and char. In an integrated coal gasification combined cycle power generation system that employs an air combustion method of using air as an oxidizing agent to generate coal gas in a gasification furnace and that supplies the coal gas to a gas turbine after separating and capturing carbon dioxide from the coal gas in a carbon-dioxide capturing device, a portion of the carbon dioxide separated and captured by the carbon-dioxide capturing device is used as a carrier gas for pulverized coal and char.
摘要翻译: 提供了一种装备有二氧化碳捕集装置的气吹综合煤气化联合循环发电系统,其中综合煤气化联合循环发电系统通过获得替代氮气的新载体源而不需要空气分离器 作为用于加压和携带粉煤和炭的载气的气体。 在一种综合煤气化联合循环发电系统中,采用利用空气作为氧化剂的空气燃烧方法在气化炉中产生煤气,并且在从煤中分离和捕获二氧化碳后将煤气供应到燃气轮机 二氧化碳捕获装置中的气体,被二氧化碳捕获装置分离和捕获的二氧化碳的一部分用作粉煤和焦炭的载气。
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公开(公告)号:US20110308230A1
公开(公告)日:2011-12-22
申请号:US13055765
申请日:2009-07-07
申请人: Soken Takase , Katsuhiro Ota , Takao Hashimoto , Tokushi Maruta , Akemi Matsuo , Hiromi Ishii
发明人: Soken Takase , Katsuhiro Ota , Takao Hashimoto , Tokushi Maruta , Akemi Matsuo , Hiromi Ishii
IPC分类号: F02C6/00
CPC分类号: F02C3/28 , C10J3/466 , C10J3/506 , C10J3/723 , C10J3/86 , C10J2300/0906 , C10J2300/0909 , C10J2300/093 , C10J2300/094 , C10J2300/0956 , C10J2300/0959 , C10J2300/1603 , C10J2300/165 , C10J2300/1653 , C10J2300/1876 , F01K23/068 , F02C6/18 , F05D2220/722 , F26B21/06 , F26B23/001 , Y02E20/16 , Y02E20/18 , Y02P70/405
摘要: Provided is an integrated coal gasification combined cycle apparatus that can operate a coal pulverizer using gas turbine exhaust gas as drying gas even when the concentration of oxygen in the gas turbine exhaust gas to be used as the drying gas is temporarily increased. In the integrated coal gasification combined cycle plant using combustion exhaust gas from a gas turbine as the drying gas for a coal pulverizer and adjusting the temperature of the drying gas by mixing outlet gas from a denitration device installed inside an exhaust gas boiler and outlet gas from the exhaust gas boiler, an auxiliary burner is started when the concentration of oxygen in the drying gas is increased to a predetermined value or more and is installed so as to adjust the concentration of oxygen in the drying gas using the combustion exhaust gas generated thereby.
摘要翻译: 提供了一种综合的煤气化联合循环装置,即使当用作干燥气体的燃气轮机废气中的氧气浓度暂时增加时,也可以使用燃气轮机废气作为干燥气体来操作煤粉碎机。 在使用来自燃气轮机的燃烧废气的综合煤气化联合循环装置中,作为用于煤粉碎机的干燥气体,并且通过混合安装在废气锅炉内的脱硝装置的出口气体和出口气体来调节干燥气体的温度 当干燥气体中的氧气浓度增加到预定值以上时,启动辅助燃烧器,并且使用由此产生的燃烧废气来调节干燥气体中的氧浓度。
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公开(公告)号:US20110126743A1
公开(公告)日:2011-06-02
申请号:US13055942
申请日:2009-08-28
申请人: Soken Takase , Katsuhiro Ota , Hiromi Ishii , Takashi Kijima
发明人: Soken Takase , Katsuhiro Ota , Hiromi Ishii , Takashi Kijima
IPC分类号: F23K1/00
CPC分类号: C10J3/466 , C10J2300/0906 , C10J2300/0909 , C10J2300/093 , C10J2300/0959 , C10J2300/1678 , C10J2300/1846 , C10J2300/1861 , C10J2300/1869 , C10J2300/1876 , C10J2300/1884 , F25J3/04545 , F25J3/04563 , F25J2260/42 , Y02E20/16 , Y02E20/18
摘要: Provided is a gasification furnace apparatus equipped with a supply source of low-oxygen-concentration drying gas that does not require fuel. A coal pulverizer that produces pulverized coal by pulverizing coal, an air separator that separates air into oxygen gas and nitrogen gas, and a gasification furnace that produces product gas by introducing thereinto the pulverized coal and the oxygen gas, are included. By receiving a supply of excess nitrogen gas from the air separator, the air diluted with nitrogen is used as a source of low-oxygen-concentration gas for drying the pulverized coal, and an air heater that heats the source of low-oxygen-concentration gas to a temperature at which drying can be performed is provided.
摘要翻译: 提供了一种装有不需要燃料的低氧浓度干燥气体供给源的气化炉装置。 包括通过粉碎煤产生粉煤的煤粉碎机,将空气分离成氧气和氮气的空气分离器,以及通过引入粉煤和氧气产生产物气体的气化炉。 通过从空气分离器接收过量的氮气,用氮气稀释的空气作为用于干燥粉煤的低氧浓度气体源,以及加热低氧浓度源的空气加热器 提供气体到能够进行干燥的温度。
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公开(公告)号:US20080295480A1
公开(公告)日:2008-12-04
申请号:US12007244
申请日:2008-01-08
申请人: Yoshinori Hyakutake , Yoshiaki Tsukuda , Takao Hashimoto , Satoshi Uchida , Katsuhiro Ota , Takashi Sonoda
发明人: Yoshinori Hyakutake , Yoshiaki Tsukuda , Takao Hashimoto , Satoshi Uchida , Katsuhiro Ota , Takashi Sonoda
CPC分类号: F02C3/28 , C10J3/00 , C10J3/466 , C10J3/723 , C10J3/84 , C10J2300/093 , C10J2300/0956 , C10J2300/0959 , C10J2300/165 , C10J2300/1671 , C10J2300/1675 , C10J2300/1678 , C10J2300/1884 , F01K23/068 , Y02E20/16 , Y02E20/18
摘要: A gasifying agent supply path A from an axial flow compressor 21 which boosts pressure of a gasifying agent to a gasifying furnace 2 is branched, and a gasifying agent bypass path D having an escaping pressure adjusting valve 23 is provided. The flow quantity or pressure of the gasifying agent supplied to the gasifying furnace 2 from the gasifying agent supply path A can be adjusted according to the degree of opening of the adjusting valve 23 disposed in the gasifying agent bypass path D, whereby providing a control valve in the gasifying agent supply path A is no longer necessary. Thus, pressure loss at the gasifying agent supply path A can be suppressed, and the discharge pressure of the axial flow compressor 21 can be greatly reduced.
摘要翻译: 来自将轴向压缩机21的气化剂供给路径A分支,气化炉2将气化剂的压力提高到气化炉2,并且设置有具有逸出压力调节阀23的气化剂旁路路径D. 从气化剂供给路径A向气化炉2供给的气化剂的流量或压力可以根据设置在气化剂旁通路径D中的调节阀23的开度而进行调整,由此提供控制阀 在气化剂供给路径A中不再需要。 因此,能够抑制气化剂供给路径A的压力损失,能够大幅降低轴流式压缩机21的排出压力。
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公开(公告)号:US20130247465A1
公开(公告)日:2013-09-26
申请号:US13819850
申请日:2012-01-24
申请人: Yoshinori Koyama , Takao Hashimoto , Katsuhiro Ota , Hiromi Ishii , Shozo Kaneko
发明人: Yoshinori Koyama , Takao Hashimoto , Katsuhiro Ota , Hiromi Ishii , Shozo Kaneko
IPC分类号: C10J3/72
CPC分类号: C10J3/723 , C10J3/485 , C10J3/721 , C10J2300/093 , C10J2300/0956 , C10J2300/1246 , C10J2300/1618 , C10J2300/165 , C10J2300/1665 , C10K3/04 , Y02E20/16 , Y02E20/18
摘要: A hydrocarbon feedstock gasifier (gasifier) is provided with: a heat transmission surface disposed within a gasification region of a gasifier configured from a pressure vessel for generating produced gas by partially oxidizing coal which is a hydrocarbon feedstock; a heat exchanger disposed on the path of a circulation line for a circulation medium circulating within the heat transmission surface and for exchanging the heat of the circulation medium; and a circulation pump for circulating the circulation medium.
摘要翻译: 烃原料气化器(气化器)设置有:传热表面,其设置在由用于通过部分氧化作为烃原料的煤产生生成气体的压力容器的气化器的气化区域内; 热交换器,设置在用于循环介质的循环管道的路径上,循环介质在所述传热表面内循环并用于交换所述循环介质的热量; 以及用于循环循环介质的循环泵。
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公开(公告)号:US08028511B2
公开(公告)日:2011-10-04
申请号:US12007244
申请日:2008-01-08
申请人: Yoshinori Hyakutake , Yoshiaki Tsukuda , Takao Hashimoto , Satoshi Uchida , Katsuhiro Ota , Takashi Sonoda
发明人: Yoshinori Hyakutake , Yoshiaki Tsukuda , Takao Hashimoto , Satoshi Uchida , Katsuhiro Ota , Takashi Sonoda
CPC分类号: F02C3/28 , C10J3/00 , C10J3/466 , C10J3/723 , C10J3/84 , C10J2300/093 , C10J2300/0956 , C10J2300/0959 , C10J2300/165 , C10J2300/1671 , C10J2300/1675 , C10J2300/1678 , C10J2300/1884 , F01K23/068 , Y02E20/16 , Y02E20/18
摘要: A gasifying agent supply path A from an axial flow compressor 21 which boosts pressure of a gasifying agent to a gasifying furnace 2 is branched, and a gasifying agent bypass path D having an escaping pressure adjusting valve 23 is provided. The flow quantity or pressure of the gasifying agent supplied to the gasifying furnace 2 from the gasifying agent supply path A can be adjusted according to the degree of opening of the adjusting valve 23 disposed in the gasifying agent bypass path D, whereby providing a control valve in the gasifying agent supply path A is no longer necessary. Thus, pressure loss at the gasifying agent supply path A can be suppressed, and the discharge pressure of the axial flow compressor 21 can be greatly reduced.
摘要翻译: 来自将轴向压缩机21的气化剂供给路径A分支,气化炉2将气化剂的压力提高到气化炉2,并且设置有具有逸出压力调节阀23的气化剂旁路路径D. 从气化剂供给路径A向气化炉2供给的气化剂的流量或压力可以根据设置在气化剂旁通路径D中的调节阀23的开度而进行调整,由此设置控制阀 在气化剂供给路径A中不再需要。 因此,能够抑制气化剂供给路径A的压力损失,能够大幅降低轴流式压缩机21的排出压力。
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公开(公告)号:US08601817B2
公开(公告)日:2013-12-10
申请号:US13389683
申请日:2010-12-09
CPC分类号: C01B3/16 , C01B2203/0475 , C01B2203/0485 , C01B2203/0883 , C01B2203/0894 , C01B2203/1614 , C01B2203/1628 , C01B2203/169 , C01B2203/84 , C10K1/004 , C10K1/005 , C10K3/04 , Y02E20/16 , Y02E20/18
摘要: A hydrogen production apparatus which includes: a humidifier (2), which is supplied with a process fluid containing carbon monoxide and mixes the process fluid with steam; a reactor (3), which reacts the humidified process fluid output from the humidifier in the presence of a catalyst, thereby converting the carbon monoxide within the process fluid into carbon dioxide; a first pipe (A) through which high-temperature process fluid flows following reaction in the reactor; a second pipe (B) that supplies makeup water; at least one first heat exchanger (51a, 51b) disposed at one of one or more locations where the first pipe and the second pipe cross each other; and a third pipe (C) that supplies steam generated by heat exchange in the first heat exchanger to other apparatus.
摘要翻译: 一种氢气制备装置,包括:加湿器(2),其供应含有一氧化碳的工艺流体并将所述工艺流体与蒸汽混合; 反应器(3),其在催化剂存在下使加湿器输出的加湿过程流体反应,从而将过程流体中的一氧化碳转化为二氧化碳; 第一管(A),高温处理流体在反应器中反应后流过其中; 供给化妆水的第二个管道(B); 至少一个第一热交换器(51a,51b)设置在第一管和第二管彼此交叉的一个或多个位置中的一个位置处; 以及将第一热交换器中通过热交换产生的蒸汽供给到其他装置的第三管道(C)。
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公开(公告)号:US08561408B2
公开(公告)日:2013-10-22
申请号:US13058150
申请日:2009-12-10
申请人: Takanori Tsutsumi , Yoshinori Koyama , Katsuhiro Ota , Takashi Fujii , Takashi Yamamoto , Hiromi Ishii
发明人: Takanori Tsutsumi , Yoshinori Koyama , Katsuhiro Ota , Takashi Fujii , Takashi Yamamoto , Hiromi Ishii
CPC分类号: F01K17/04 , C01B3/14 , C01B3/16 , C01B2203/0883 , C01B2203/0894 , C01B2203/1294 , F01K23/064 , Y02E20/18 , Y02E20/326 , Y02P20/13
摘要: The amount of high-temperature steam supplied from external equipment is reduced. Provided is a hydrogen production system (1) including a reactor (3) that allows a humidified process fluid output from a humidifier (2) to react in the presence of a catalyst to transform carbon monoxide in the process fluid into carbon dioxide; a second channel (B) through which the high-temperature process fluid that has reacted in the reactor (3) flows; a circulation channel (C) through which excess water in the humidifier (2) is circulated; and a first heat exchanger (7), disposed at an intersection of the circulation channel (C) and the second channel (B), for heat exchange between the high-temperature process fluid that has reacted in the reactor (3) and the fluid circulated through the circulation channel (C).
摘要翻译: 从外部设备供应的高温蒸汽量减少。 提供了一种氢生产系统(1),其包括反应器(3),其允许从加湿器(2)输出的加湿过程流体在催化剂存在下反应以将过程流体中的一氧化碳转化为二氧化碳; 在反应器(3)中已经反应的高温处理流体流过的第二通道(B); 循环通道(C),加湿器(2)中的多余的水循环通过; 和设置在循环通道(C)和第二通道(B)的交点处的第一热交换器(7),用于在反应器(3)中反应的高温处理流体与流体 循环通过循环通道(C)。
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公开(公告)号:US20120137689A1
公开(公告)日:2012-06-07
申请号:US13389683
申请日:2010-12-09
IPC分类号: F01K21/04
CPC分类号: C01B3/16 , C01B2203/0475 , C01B2203/0485 , C01B2203/0883 , C01B2203/0894 , C01B2203/1614 , C01B2203/1628 , C01B2203/169 , C01B2203/84 , C10K1/004 , C10K1/005 , C10K3/04 , Y02E20/16 , Y02E20/18
摘要: A hydrogen production apparatus (1) which, in order to improve power generation efficiency, comprises: a humidifier (2), which is supplied with a process fluid containing carbon monoxide and mixes the process fluid with steam; a reactor (3), which reacts the humidified process fluid output from the humidifier (2) in the presence of a catalyst, thereby converting the carbon monoxide within the process fluid into carbon dioxide; a first pipe (A) through which the high-temperature process fluid flows following reaction in the reactor (3); a second pipe (B) that supplies makeup water; at least one first heat exchanger (51a, 51b), each of which is disposed at one of one or more locations where the first pipe (A) and the second pipe (B) cross each other; and a third pipe (C) that supplies the steam generated by heat exchange in the first heat exchanger (51a, 51b) to other apparatus.
摘要翻译: 为了提高发电效率的氢制造装置(1)包括:加湿器(2),其供给含有一氧化碳的工艺流体并将工艺流体与蒸汽混合; 反应器(3),其在催化剂存在下使加湿器(2)输出的加湿过程流体反应,从而将过程流体中的一氧化碳转化为二氧化碳; 第一管(A),高温处理流体在反应器(3)中反应后流过其中; 供给化妆水的第二个管道(B); 至少一个第一热交换器(51a,51b),每个第一热交换器设置在第一管(A)和第二管(B)彼此交叉的一个或多个位置中的一个处; 以及将第一热交换器(51a,51b)中通过热交换产生的蒸汽供给到其他装置的第三配管(C)。
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公开(公告)号:US20110314814A1
公开(公告)日:2011-12-29
申请号:US13058150
申请日:2009-12-10
申请人: Takanori Tsutsumi , Yoshinori Koyama , Katsuhiro Ota , Takashi Fujii , Takashi Yamamoto , Hiromi Ishii
发明人: Takanori Tsutsumi , Yoshinori Koyama , Katsuhiro Ota , Takashi Fujii , Takashi Yamamoto , Hiromi Ishii
CPC分类号: F01K17/04 , C01B3/14 , C01B3/16 , C01B2203/0883 , C01B2203/0894 , C01B2203/1294 , F01K23/064 , Y02E20/18 , Y02E20/326 , Y02P20/13
摘要: The amount of high-temperature steam supplied from external equipment is reduced. Provided is a hydrogen production system (1) including a reactor (3) that allows a humidified process fluid output from a humidifier (2) to react in the presence of a catalyst to transform carbon monoxide in the process fluid into carbon dioxide; a second channel (B) through which the high-temperature process fluid that has reacted in the reactor (3) flows; a circulation channel (C) through which excess water in the humidifier (2) is circulated; and a first heat exchanger (7), disposed at an intersection of the circulation channel (C) and the second channel (B), for heat exchange between the high-temperature process fluid that has reacted in the reactor (3) and the fluid circulated through the circulation channel (C).
摘要翻译: 从外部设备供应的高温蒸汽量减少。 提供了一种氢生产系统(1),其包括反应器(3),其允许从加湿器(2)输出的加湿过程流体在催化剂存在下反应以将过程流体中的一氧化碳转化为二氧化碳; 在反应器(3)中已经反应的高温处理流体流过的第二通道(B); 循环通道(C),加湿器(2)中的多余的水循环通过; 和设置在循环通道(C)和第二通道(B)的交点处的第一热交换器(7),用于在反应器(3)中反应的高温处理流体与流体 循环通过循环通道(C)。
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