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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: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: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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公开(公告)号:US20110116979A1
公开(公告)日:2011-05-19
申请号:US13002109
申请日:2009-07-10
IPC分类号: B01J8/00
CPC分类号: C10J3/02 , C10J3/485 , C10J2300/093 , C10J2300/0956 , C10J2300/0959 , C10J2300/0973 , C10J2300/0976 , C10J2300/1838 , C10J2300/1853 , C10J2300/1884 , C10J2300/1892 , C10K1/04 , Y02E20/18
摘要: Provided is a coal gasifier enabling a reduction in size of a shift reactor by generating hydrogen-rich gasified coal gas. In a coal gasifier generating gasified coal gas by a gasification reaction proceeding in a furnace fed with a gasifiable raw material, such as coal, and a gasifying agent, at least one of water and steam is fed to the furnace as a material accelerating a hydrogen-generating reaction that proceeds simultaneously with the gasification reaction.
摘要翻译: 提供一种煤气化器,其能够通过产生富氢气化煤气来减小换档反应器的尺寸。 在通过气化反应进行气化反应的煤气化炉中,在气化原料如煤和气化炉中进行气化反应,将水和蒸汽中的至少一种作为加速氢气的材料供给到炉中 与气化反应同时进行的生成反应。
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公开(公告)号:US20100175364A1
公开(公告)日:2010-07-15
申请号:US12452352
申请日:2008-11-06
申请人: Takashi Yamamoto , Katsuhiro Ota , Hiromi Ishii , Yoshinori Koyama , Kimishiro Tokuda , Isao Mochida , Tatsuro Harada
发明人: Takashi Yamamoto , Katsuhiro Ota , Hiromi Ishii , Yoshinori Koyama , Kimishiro Tokuda , Isao Mochida , Tatsuro Harada
CPC分类号: F02C3/28 , C10J3/00 , C10J3/466 , C10J3/482 , C10J3/82 , C10J2300/0903 , C10J2300/0909 , C10J2300/093 , C10J2300/0986 , C10J2300/1246 , C10J2300/165 , C10J2300/1675 , C10J2300/1892 , F01K9/003 , F01K17/06 , F01K23/067 , F02C6/18 , F02C7/224 , Y02E20/18
摘要: An integrated coal gasification combined cycle facility is provided that can prevent a reduction in power generation efficiency even when low-grade coal having a relatively-high moisture content is used. Included are: a gasification section that gasifies supplied coal; a gas power generation section that generates power by using gas supplied from the gasification section; a steam power generation section that generates power by using the heat of exhaust gas discharged from the gas power generation section; and a coal drying unit that dries the coal by using exhaust heat discharged from the steam power generation section and that supplies the dried coal to the gasification section.
摘要翻译: 提供了一种综合的煤气化联合循环设备,即使使用具有相对高含水量的低等级煤,也能够防止发电效率降低。 包括:气化煤气供气; 通过使用从气化部供给的气体来发电的燃气发电部; 蒸汽发电部,其利用从所述燃气发电部排出的排气的热量来发电; 以及煤干燥单元,其通过使用从蒸汽发电部排出的废热将煤干燥并将干燥的煤供给到气化部。
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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:US08615981B2
公开(公告)日:2013-12-31
申请号:US12452352
申请日:2008-11-06
申请人: Takashi Yamamoto , Katsuhiro Ota , Hiromi Ishii , Yoshinori Koyama , Kimishiro Tokuda , Isao Mochida , Tatsuro Harada
发明人: Takashi Yamamoto , Katsuhiro Ota , Hiromi Ishii , Yoshinori Koyama , Kimishiro Tokuda , Isao Mochida , Tatsuro Harada
CPC分类号: F02C3/28 , C10J3/00 , C10J3/466 , C10J3/482 , C10J3/82 , C10J2300/0903 , C10J2300/0909 , C10J2300/093 , C10J2300/0986 , C10J2300/1246 , C10J2300/165 , C10J2300/1675 , C10J2300/1892 , F01K9/003 , F01K17/06 , F01K23/067 , F02C6/18 , F02C7/224 , Y02E20/18
摘要: An integrated coal gasification combined cycle facility is provided that can prevent a reduction in power generation efficiency even when low-grade coal having a relatively-high moisture content is used. Included are: a gasification section that gasifies supplied coal; a gas power generation section that generates power by using gas supplied from the gasification section; a steam power generation section that generates power by using the heat of exhaust gas discharged from the gas power generation section; and a coal drying unit that dries the coal by using exhaust heat discharged from the steam power generation section and that supplies the dried coal to the gasification section.
摘要翻译: 提供了一种综合的煤气化联合循环设备,即使使用具有相对高含水量的低等级煤,也能够防止发电效率降低。 包括:气化煤气供气; 通过使用从气化部供给的气体来发电的燃气发电部; 蒸汽发电部,其利用从所述燃气发电部排出的排气的热量来发电; 以及煤干燥单元,其通过使用从蒸汽发电部排出的废热将煤干燥并将干燥的煤供给到气化部。
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公开(公告)号:US08607716B2
公开(公告)日:2013-12-17
申请号:US12452134
申请日:2008-06-18
申请人: Yoshinori Koyama , Takeshi Aruga , Hiromi Ishii , Kazuyuki Myoyo
发明人: Yoshinori Koyama , Takeshi Aruga , Hiromi Ishii , Kazuyuki Myoyo
CPC分类号: F23D1/00 , C10J3/506 , C10J2200/09 , C10J2200/152 , C10J2300/093 , C10J2300/0956 , C10J2300/165 , C10J2300/1675 , C10J2300/1687 , C10J2300/1892 , Y02E20/16 , Y02E20/18
摘要: In a burner for highly caking coal in which a solid fuel channel and a gasifying agent channel are provided in a double pipe structure, the temperature increase of the particles of a highly caking solid fuel and the resulting fusion and expansion of the particles are prevented or suppressed, thereby enabling a stable operation of the gasifier. In a burner for highly caking coal in which a solid fuel channel that is attached for gasifying a highly caking solid fuel that has been pulverized into particles and that supplies the solid fuel into the gasifier, and a gasifying agent channel that supplies a gasifying agent into the gasifier are provided in a double pipe structure, the burner has a triple pipe structure including a cooling water channel that circulates cooling water between the solid fuel channel and the gasifying agent channel, and the cooling water is recovered after use.
摘要翻译: 在双重管结构中设置有固体燃料通道和气化剂通道的高结块煤的燃烧器中,防止了高结块固体燃料的颗粒的温度升高以及由此导致的颗粒的熔化和膨胀, 从而能够使气化炉稳定运转。 在用于高结块煤的燃烧器中,其中附着有固体燃料通道,用于气化已经粉碎成颗粒的高结块固体燃料并将固体燃料供应到气化器中;以及气化剂通道,其将气化剂供应到 气化器设置在双管结构中,燃烧器具有三管结构,其包括在固体燃料通道和气化剂通道之间循环冷却水的冷却水通道,并且冷却水在使用后回收。
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公开(公告)号:US20070144712A1
公开(公告)日:2007-06-28
申请号:US11643671
申请日:2006-12-22
申请人: Yoshinori Koyama , Katsuhiko Yokohama , Osamu Shinada , Hiromi Ishii , Yuichiro Kitagawa , Kosei Manabe
发明人: Yoshinori Koyama , Katsuhiko Yokohama , Osamu Shinada , Hiromi Ishii , Yuichiro Kitagawa , Kosei Manabe
CPC分类号: F28F9/22 , F22B1/18 , F22B1/1846 , F28D7/0041 , F28D7/06 , F28F13/06 , F28F19/00
摘要: A compact pressurized high-temperature gas cooler having superior heat exchange performance and excellent economical efficiency is provided. A return-flow structure is formed in which a flue through which high-temperature gas flows is formed in a pressure container, a heat exchanger is disposed in the flue, and a partition dividing the internal cross-sectional area of the flue is provided so that the high-temperature gas supplied from a bottom or a top portion of the pressure container flows back in a return direction. The cross-sectional-area division ratio dividing the internal cross-section of the flue is set so that the flow rate of the high-temperature gas flowing in one direction matches that flowing in the direction opposite thereto.
摘要翻译: 提供了具有优异的热交换性能和优异的经济效率的紧凑型加压高温气体冷却器。 形成回流结构,其中在压力容器中形成高温气体流过的烟道,在烟道中设置热交换器,并且设置分隔烟道的内部横截面积的分隔件 从压力容器的底部或顶部供应的高温气体沿返回方向回流。 设定分割烟道内部截面的截面积分割比,使得在一个方向上流动的高温气体的流量与沿其相反方向流动的流量相匹配。
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