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公开(公告)号：US08505472B2
公开(公告)日：2013-08-13
申请号：US12160492
申请日：2007-01-10
申请人： Yuki Kamikawa , Masayuki Taniguchi , Hisayuki Orita , Hironobu Kobayashi , Akira Baba , Toshihiko Mine , Shinichirou Nomura , Noriyuki Ooyatsu , Satoshi Tadakuma , Hidehisa Yoshizako , Hiroaki Kanemoto , Kouji Kuramashi , Akihito Orii , Shinji Tsuda , Hirofumi Okazaki , Takanori Yano , Katsumi Shimohira
发明人： Yuki Kamikawa , Masayuki Taniguchi , Hisayuki Orita , Hironobu Kobayashi , Akira Baba , Toshihiko Mine , Shinichirou Nomura , Noriyuki Ooyatsu , Satoshi Tadakuma , Hidehisa Yoshizako , Hiroaki Kanemoto , Kouji Kuramashi , Akihito Orii , Shinji Tsuda , Hirofumi Okazaki , Takanori Yano , Katsumi Shimohira
CPC分类号： F23N3/002 , F22B1/22 , F23B5/02 , F23C5/28 , F23C7/008 , F23C7/04 , F23D1/005 , F23L9/04 , F23L13/06 , Y02E20/328
摘要： A pulverized coal-fired boiler efficiently supplies air to a central part of a furnace and the neighborhood of a furnace wall, thereby promoting mixture with combustion gas, and reducing both NOx and CO.The main after air ports are structured so as to jet air having a large momentum for enabling arrival at the central part of the furnace, and the sub-after air ports are structured so as to jet air having a small momentum to the neighborhood of the wall face of the furnace, and a sectional center of each of the sub-after air ports is within a range from 1 to 5 times of a caliber of the main after air ports from a sectional center of each of the main after air ports.
摘要翻译： 粉煤燃烧锅炉有效地向炉的中心部分和炉壁附近供应空气，从而促进与燃烧气体的混合，并且还可以减少NOx和CO。主后气道被构造成喷射空气 具有能够到达炉的中心部的大动量，并且副后空气构造成将具有小动量的空气喷射到炉壁面附近，并且每个 次后空气口的主后排气口的距离为主后排气口的口径的1〜5倍的范围。
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公开(公告)号：US20100224108A1
公开(公告)日：2010-09-09
申请号：US12160492
申请日：2007-01-10
申请人： Yuki Kamikawa , Masayuki Taniguchi , Hisayuki Orita , Hironobu Kobayashi , Akira Baba , Toshihiko Mine , Shinichirou Nomura , Noriyuki Ooyatsu , Satoshi Tadakuma , Hidehisa Yoshizako , Hiroaki Kanemoto , Kouji Kuramashi , Akihito Orii , Shinji Tsuda , Hirofumi Okazaki , Takanori Yano , Katsumi Shimohira
发明人： Yuki Kamikawa , Masayuki Taniguchi , Hisayuki Orita , Hironobu Kobayashi , Akira Baba , Toshihiko Mine , Shinichirou Nomura , Noriyuki Ooyatsu , Satoshi Tadakuma , Hidehisa Yoshizako , Hiroaki Kanemoto , Kouji Kuramashi , Akihito Orii , Shinji Tsuda , Hirofumi Okazaki , Takanori Yano , Katsumi Shimohira
CPC分类号： F23N3/002 , F22B1/22 , F23B5/02 , F23C5/28 , F23C7/008 , F23C7/04 , F23D1/005 , F23L9/04 , F23L13/06 , Y02E20/328
摘要： A pulverized coal-fired boiler efficiently supplies air to a central part of a furnace and the neighborhood of a furnace wall, thereby promoting mixture with combustion gas, and reducing both NOx and CO.The main after air ports are structured so as to jet air having a large momentum for enabling arrival at the central part of the furnace, and the sub-after air ports are structured so as to jet air having a small momentum to the neighborhood of the wall face of the furnace, and a sectional center of each of the sub-after air ports is within a range from 1 to 5 times of a caliber of the main after air ports from a sectional center of each of the main after air ports.
摘要翻译： 粉煤燃烧锅炉有效地向炉的中心部分和炉壁附近供应空气，从而促进与燃烧气体的混合，并且还可以减少NOx和CO。主后气道被构造成喷射空气 具有能够到达炉的中心部的大动量，并且副后空气构造成将具有小动量的空气喷射到炉壁面附近，并且每个 次后空气口的主后排气口的距离为主后排气口的口径的1〜5倍的范围。
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公开(公告)号：US20110197831A1
公开(公告)日：2011-08-18
申请号：US12594997
申请日：2008-04-11
CPC分类号： G01F1/74 , F22B35/00 , F23D1/00 , F23N1/022 , F23N2039/02 , F23N2041/10 , G01F1/666 , G01F1/7046 , G01F1/712 , G01P5/22
摘要： A pulverized coal burning boiler is provided, which reduces an air-excess ratio thereby to reduce the emission of unburned contents such as CO. The pulverized coal burning boiler includes a pulverized coal feed measuring device for measuring the feeding rates of the pulverized coal to be conveyed through coal feeding pipes, individually, and a control device for calculating the burning air feeding rates to match the pulverized coal feeding rates thereby to send a control command signal to burning air feed adjusting device, so that a burner air ratio set by a burner air ratio setting device may be kept on the basis of both the pulverized coal feeding rate, which is measured by the pulverized coal feed measuring device, and the burning air feeding rate, which is measured by the burning air feeding rate measuring device and fed to a pulverized coal burner connected to the coal feeding pipes.
摘要翻译： 提供了一种粉煤燃烧锅炉，其减少了空气过剩比例，从而减少了诸如CO的未燃烧内容物的排放。粉煤燃烧锅炉包括用于测量粉煤供料速率的粉煤进料测量装置 通过供煤管单独输送，以及用于计算燃烧空气供给速度以匹配粉煤供给速率的控制装置，从而向燃烧空气供给调节装置发送控制指令信号，使得由燃烧器设定的燃烧器空气比 空气比设定装置可以基于由粉煤供给测量装置测量的粉煤供给速度和通过燃烧空气供给速度测量装置测量的供给燃烧空气的燃烧空气进给速度的燃烧空气供给速率， 连接到供煤管的煤粉燃烧器。
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4.发明授权Fuel distribution device for fuel feed ducts and method of operating distribution device 失效用于燃料供给管道的燃料分配装置和操作分配装置的方法公开(公告)号：US06976440B2
公开(公告)日：2005-12-20
申请号：US10468956
申请日：2001-12-03
申请人： Yoshinori Ohtani , Hidehisa Yoshizako , Hiroaki Kanemoto , Yutaka Takeno , Yoshio Shimogori , Toshikazu Tsumura , Yoshitaka Takahashi
发明人： Yoshinori Ohtani , Hidehisa Yoshizako , Hiroaki Kanemoto , Yutaka Takeno , Yoshio Shimogori , Toshikazu Tsumura , Yoshitaka Takahashi
CPC分类号： F23C7/008 , F23C5/28 , F23K3/02 , F23K2201/30 , F23K2203/105 , F23K2203/201
摘要： A fuel supply duct, which supplies a mixed fluid of a solid fuel and carrier gas to one or more burners provided on the walls of a furnace, is provided with a branching part, and each of a plurality of branch ducts, which branch out from the branching part, is connected to a corresponding burner. Also a damper, with which the tilt angle with respect to the direction of flow of the mixed fluid can be changed, is positioned in the fuel supply duct at the upstream side of the branching part so that a mutual difference will arise in the solid fuel concentrations of the mixed fluid supplied to the respective branch ducts. A fuel distributor for fuel supply duct is thus arranged. The tilt angle of the above-mentioned damper is adjusted to increase the concentration of solid fuel in the mixed fluid supplied to a specific burner. At a burner to which the high solid fuel concentration is supplied, stability of ignition and stable combustion of the ignited flame can be obtained during low load operation.
摘要翻译： 将设置在炉壁上的一个或多个燃烧器供给固体燃料和载气的混合流体的燃料供给管道设置有分支部，分支部分分支出多个分支管道 分支部分连接到相应的燃烧器。 另外，可以改变相对于混合流体的流动方向的倾斜角度的阻尼器位于分支部分的上游侧的燃料供应管道中，使得固体燃料中将产生相互的差异 供给各分支管道的混合流体的浓度。 因此布置了用于燃料供应管道的燃料分配器。 调节上述阻尼器的倾斜角度以增加供应给特定燃烧器的混合流体中固体燃料的浓度。 在供应高固体燃料浓度的燃烧器中，在低负载运行期间可以获得点火稳定性和点燃火焰的稳定燃烧。
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公开(公告)号：US09513000B2
公开(公告)日：2016-12-06
申请号：US13825157
申请日：2011-09-29
IPC分类号： F23L7/00 , F23J15/02 , F23D14/66 , F23C9/00 , F01K7/40 , F22B1/18 , F23J15/06 , F23C9/08 , F23L15/04
CPC分类号： F23L7/007 , F01K7/40 , F22B1/18 , F23C9/00 , F23C9/08 , F23D14/66 , F23J15/022 , F23J15/06 , F23J2215/50 , F23L15/04 , Y02E20/322 , Y02E20/326 , Y02E20/344 , Y02E20/348
摘要： An oxygen combustion system includes a boiler to burn fuel using combustion gas composed of oxygen-rich gas and circulating flue gas, a dust remover disposed in a flue through which flue gas discharged from the boiler flows, a second flue leading the combustion gas to the boiler, the combustion gas being made by mixing the circulating flue gas extracted downstream of the dust remover with the oxygen-rich gas, a combustion gas heater exchanging heat between the flue gas flowing between the boiler and dust remover and the combustion gas flowing through the second flue, and a flue gas cooler disposed between the heater and the dust remover to cool the flue gas. A control unit controls at least one of a flow rate and cooling medium temperature of the flue gas cooler such that temperature of the flue gas introduced into the dust remover will be between 90° C. and 140° C.
摘要翻译： 氧气燃烧系统包括使用由富氧气体和循环烟道气组成的燃烧气体燃烧燃料的锅炉，设置在烟道中排出的烟道的除尘器，通过该烟道排出烟道气流过的第二烟道， 锅炉，通过将从除尘器下游提取的循环烟道气与富氧气体混合而形成的燃烧气体，在锅炉和除尘器之间流动的烟道气与流过锅炉的燃烧气体之间交换热量的燃烧气体加热器 第二烟道和布置在加热器和除尘器之间的烟道气体冷却器以冷却烟道气。 控制单元控制烟气冷却器的流量和冷却介质温度中的至少一个，使得引入除尘器的烟道气的温度将在90℃和140℃之间。
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公开(公告)号：US20120272626A1
公开(公告)日：2012-11-01
申请号：US13509693
申请日：2010-11-19
申请人： Yoshiaki Mitsui , Hidehisa Yoshizako , Noriyuki Imada , Naoki Oda
发明人： Yoshiaki Mitsui , Hidehisa Yoshizako , Noriyuki Imada , Naoki Oda
IPC分类号： B01D50/00
CPC分类号： F23L7/007 , B01D53/343 , B01D53/346 , B01D53/504 , B01D53/508 , B01D53/56 , B01D53/62 , B01D53/75 , B01D2251/304 , B01D2251/306 , B01D2251/404 , B01D2251/606 , B01D2257/302 , B01D2257/404 , B01D2257/504 , F23C9/003 , F23J15/006 , F23J15/06 , F23J15/08 , F23J2215/20 , F23J2215/50 , F23J2217/10 , F23J2217/50 , F23J2219/20 , F23J2219/70 , Y02E20/326 , Y02E20/344 , Y02E20/346 , Y02E20/348 , Y02E20/363
摘要： In an exhaust gas treatment device provided with: an exhaust gas treatment unit in which an oxygen combustion boiler 1 using coal as fuel, a denitration device 3, an air preheater 4, a dust-collection device 5, a desulfurization device 6, and a carbon dioxide recovery device 8 are sequentially arranged from the upstream side to the downstream side of an exhaust gas duct; and an exhaust gas circulation unit which branches off from the exhaust gas duct at an outlet of the dust-collection device 5 or an outlet of the desulfurization device 6 and through which the exhaust gas is preheated by the air preheater 4 and returned to the oxygen combustion boiler 1, a heat-recovery heat exchanger 13 that adjusts a gas temperature at an inlet of the dust-collection device 5 to be not greater than an acid dew point of SO3 and not lower than a water dew point is provided between the air preheater 4 and the dust-collection device 5, a reheating heat exchanger 13 that adjusts a gas temperature to be not lower than the acid dew point of SO3 is provided in the vicinity of a branch of the exhaust gas circulation unit, adjusting the gas temperature at the inlet of the dust-collection device 4 to be not greater than the acid dew point of SO3 makes it possible to prevent corrosion of pipes in the exhaust gas circulation unit and to avoid a decrease in fluidity or combustibility of the pulverized coal in the pipes in the mill.
摘要翻译： 在具有：利用煤作为燃料的氧气燃烧锅炉1，脱硝装置3，空气预热器4，集尘装置5，脱硫装置6以及脱硫装置6的废气处理装置的排气处理装置中， 二氧化碳回收装置8从废气导管的上游侧向下游侧依次配置; 以及废气循环单元，其在集尘装置5的出口或脱硫装置6的出口处从废气导管分支，并且废气通过空气预热器4预热并返回到氧气 燃烧锅炉1，将在尘埃捕集装置5的入口处的气体温度调节为不大于SO3的酸露点且不低于露点的热回收热交换器13设置在空气 预热器4和集尘装置5，在废气循环装置的分支附近设置有调节不低于SO3的酸露点的气体温度的再热交换器13，调整气体温度 在集尘装置4的入口处不大于SO3的酸露点使得可以防止废气循环装置中管道的腐蚀并避免流动性或可燃性的降低 在磨机管道中的粉煤。
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7.发明申请Drying Conveyer, and Thermal Electric Power Generation System Provided with Same 审中-公开干燥输送机，以及与此相同的热发电系统公开(公告)号：US20140290251A1
公开(公告)日：2014-10-02
申请号：US14233621
申请日：2012-07-18
申请人： Mitsugu Sugasawa , Hidehisa Yoshizako , Terufumi Miyata , Takahiro Okada , Yoshinori Taoka , Shunichi Sato
发明人： Mitsugu Sugasawa , Hidehisa Yoshizako , Terufumi Miyata , Takahiro Okada , Yoshinori Taoka , Shunichi Sato
IPC分类号： C10B57/10
CPC分类号： C10B57/10 , F23G5/05 , F23K1/00 , F23K1/04 , F23K2201/20 , F23K2203/103 , F23K2203/104 , F26B3/08 , F26B17/04 , Y02E20/12
摘要： [Problem] To provide a drying conveyer apparatus capable of efficiently and uniformly drying coarse particles.[Solution] The present invention is characterized in that a gas get portion (29) is provided on a bottom part of a conveyance member (25), a wind box (35) is provided for supplying drying gas (49) from blow the conveyance member (25), an object to be conveyed (2) is inputted within the conveyance member (25), the drying gas (35) is jetted from the gas jet portion (29) into the conveyance member (25) when the conveyance member (25) passes over the wind box (35), and the object to be conveyed (2) is dried while a fluidized bed thereof is formed.
摘要翻译： 提供能够高效均匀地干燥粗颗粒的干燥输送装置。 [解决方案]本发明的特征在于，在输送构件（25）的底部设置有气体获取部（29），设置有风箱（35），用于从吹送输送 （25）中，输送物（2）输入到输送部件（25）内，当输送部件（25）从输送部件（25）喷出干燥气体 （25）通过风箱（35），并且在形成流化床的同时将被输送物体（2）干燥。
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公开(公告)号：US08778041B2
公开(公告)日：2014-07-15
申请号：US13509693
申请日：2010-11-19
申请人： Yoshiaki Mitsui , Hidehisa Yoshizako , Noriyuki Imada , Naoki Oda
发明人： Yoshiaki Mitsui , Hidehisa Yoshizako , Noriyuki Imada , Naoki Oda
IPC分类号： B01D50/00 , B01D39/20 , B01D39/06 , B01D39/14 , B01D24/00 , B01D53/34 , F23J15/08 , B01D53/50 , B01D53/75 , F23L7/00 , F23J15/06 , F23J15/00 , F23C9/00 , B01D53/56 , B01D53/62
CPC分类号： F23L7/007 , B01D53/343 , B01D53/346 , B01D53/504 , B01D53/508 , B01D53/56 , B01D53/62 , B01D53/75 , B01D2251/304 , B01D2251/306 , B01D2251/404 , B01D2251/606 , B01D2257/302 , B01D2257/404 , B01D2257/504 , F23C9/003 , F23J15/006 , F23J15/06 , F23J15/08 , F23J2215/20 , F23J2215/50 , F23J2217/10 , F23J2217/50 , F23J2219/20 , F23J2219/70 , Y02E20/326 , Y02E20/344 , Y02E20/346 , Y02E20/348 , Y02E20/363
摘要： In an exhaust gas treatment device provided with: an exhaust gas treatment unit in which an oxygen combustion boiler 1 using coal as fuel, a denitration device 3, an air preheater 4, a dust-collection device 5, a desulfurization device 6, and a carbon dioxide recovery device 8 are sequentially arranged from the upstream side to the downstream side of an exhaust gas duct; and an exhaust gas circulation unit which branches off from the exhaust gas duct at an outlet of the dust-collection device 5 or an outlet of the desulfurization device 6 and through which the exhaust gas is preheated by the air preheater 4 and returned to the oxygen combustion boiler 1, a heat-recovery heat exchanger 13 that adjusts a gas temperature at an inlet of the dust-collection device 5 to be not greater than an acid dew point of SO3 and not lower than a water dew point is provided between the air preheater 4 and the dust-collection device 5, a reheating heat exchanger 13 that adjusts a gas temperature to be not lower than the acid dew point of SO3 is provided in the vicinity of a branch of the exhaust gas circulation unit, adjusting the gas temperature at the inlet of the dust-collection device 4 to be not greater than the acid dew point of SO3 makes it possible to prevent corrosion of pipes in the exhaust gas circulation unit and to avoid a decrease in fluidity or combustibility of the pulverized coal in the pipes in the mill.
摘要翻译： 在具有：利用煤作为燃料的氧气燃烧锅炉1，脱硝装置3，空气预热器4，集尘装置5，脱硫装置6以及脱硫装置6的废气处理装置的排气处理装置中， 二氧化碳回收装置8从废气导管的上游侧向下游侧依次配置; 以及废气循环单元，其在集尘装置5的出口或脱硫装置6的出口处从废气导管分支，并且废气通过空气预热器4预热并返回到氧气 燃烧锅炉1，将在尘埃捕集装置5的入口处的气体温度调节为不大于SO3的酸露点且不低于露点的热回收热交换器13设置在空气 预热器4和集尘装置5，在废气循环装置的分支附近设置有调节不低于SO3的酸露点的气体温度的再热交换器13，调整气体温度 在集尘装置4的入口处不大于SO3的酸露点使得可以防止废气循环装置中管道的腐蚀并避免流动性或可燃性的降低 在磨机管道中的粉煤。
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公开(公告)号：US20130244190A1
公开(公告)日：2013-09-19
申请号：US13825157
申请日：2011-09-29
CPC分类号： F23L7/007 , F01K7/40 , F22B1/18 , F23C9/00 , F23C9/08 , F23D14/66 , F23J15/022 , F23J15/06 , F23J2215/50 , F23L15/04 , Y02E20/322 , Y02E20/326 , Y02E20/344 , Y02E20/348
摘要： An oxygen combustion system includes a boiler to burn fuel using combustion gas composed of oxygen-rich gas and circulating flue gas, a dust remover disposed in a flue through which flue gas discharged from the boiler flows, a second flue leading the combustion gas to the boiler, the combustion gas being made by mixing the circulating flue gas extracted downstream of the dust remover with the oxygen-rich gas, a combustion gas heater exchanging heat between the flue gas flowing between the boiler and dust remover and the combustion gas flowing through the second flue, and a flue gas cooler disposed between the heater and the dust remover to cool the flue gas. A control unit controls at least one of a flow rate and cooling medium temperature of the flue gas cooler such that temperature of the flue gas introduced into the dust remover will be between 90° C. and 140° C.
摘要翻译： 氧气燃烧系统包括使用由富氧气体和循环烟道气组成的燃烧气体燃烧燃料的锅炉，设置在烟道中排出的烟道的除尘器，通过该烟道排出烟道气流过的第二烟道， 锅炉，通过将从除尘器下游提取的循环烟道气与富氧气体混合而形成的燃烧气体，在锅炉和除尘器之间流动的烟道气与流过锅炉的燃烧气体之间交换热量的燃烧气体加热器 第二烟道和布置在加热器和除尘器之间的烟道气体冷却器以冷却烟道气。 控制单元控制烟气冷却器的流量和冷却介质温度中的至少一个，使得引入除尘器的烟道气的温度将在90℃和140℃之间。
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