公开(公告)号：US20080230444A1

公开(公告)日：2008-09-25

申请号：US10586439

申请日：2005-01-27

申请人： Yuki Iwadate ,  Takao Kobayashi ,  Seiichiro Toyoda ,  Takashi Imaizumi ,  Fumiaki Morozumi

发明人： Yuki Iwadate ,  Takao Kobayashi ,  Seiichiro Toyoda ,  Takashi Imaizumi ,  Fumiaki Morozumi

IPC分类号： C10G9/00 ,  B01J19/00

CPC分类号： C01B3/34 ,  C01B3/24 ,  C01B2203/0227 ,  C01B2203/0266 ,  C01B2203/04 ,  C01B2203/0425 ,  C01B2203/0475 ,  C01B2203/0485 ,  C01B2203/0816 ,  C01B2203/0822 ,  C01B2203/0827 ,  C01B2203/0877 ,  C01B2203/1247 ,  C10G9/20 ,  C10J3/482 ,  C10J3/56 ,  C10J3/66 ,  C10J2300/09 ,  C10J2300/0916 ,  C10J2300/0956 ,  C10J2300/0983 ,  C10J2300/1207 ,  C10J2300/1215 ,  C10J2300/16 ,  C10K3/008 ,  Y02P20/128 ,  Y02P20/129

摘要： A hydrocarbon material processing system can reduce consumption of fossil fuel, environmental loads, and cost for processing a hydrocarbon material. The hydrocarbon material processing system has a gasification furnace (10) for pyrolyzing and gasifying wastes (51), waste plastics (52), pyrolysis tar (53), residual hydrocarbon heavy oil (54), and organic matter such as biomass (55) to produce a heat source gas. The hydrocarbon material processing system also has a cracking furnace (101) for thermally cracking a hydrocarbon material by using the heat source gas produced in the gasification furnace (10).

摘要翻译： 烃类材料处理系统可以减少化石燃料的消耗，环境负荷以及加工烃类材料的成本。 烃类材料处理系统具有用于热解和气化废物（51），废塑料（52），热解焦油（53），残余烃重油（54）和有机物质如生物质（55）的气化炉（10） 以产生热源气体。 烃材料处理系统还具有通过使用在气化炉（10）中产生的热源气体来热裂化烃材料的裂解炉（101）。

公开(公告)号：US20060137579A1

公开(公告)日：2006-06-29

申请号：US10563434

申请日：2004-07-23

申请人： Hiroyuki Fujimura ,  Takahiro Oshita ,  Norihisa Miyoshi ,  Seiichiro Toyoda ,  Kei Matsuoka ,  Tatsuya Hasegawa

发明人： Hiroyuki Fujimura ,  Takahiro Oshita ,  Norihisa Miyoshi ,  Seiichiro Toyoda ,  Kei Matsuoka ,  Tatsuya Hasegawa

IPC分类号： F23G5/00 ,  F23B30/00

CPC分类号： F23G5/027 ,  F23C13/08 ,  F23G5/006 ,  F23G5/0276 ,  F23G5/16 ,  F23G5/30 ,  F23G5/46 ,  F23G2201/303 ,  F23G2201/304 ,  F23G2202/101 ,  F23G2202/104 ,  F23G2203/502 ,  F23G2209/262 ,  F23J15/006 ,  F23J15/06 ,  F23J2217/50 ,  F23L2900/07002 ,  F23L2900/07005 ,  Y02E20/344 ,  Y02E20/363

摘要： A gasification system has a gasification furnace (1) for gasifying wastes to produce a combustible gas and a combustion furnace (2) for combusting char and/or tar produced by gasification in the gasification furnace (1). The gasification system also has a return line for returning a combustion gas discharged from the combustion furnace (2) to the gasification furnace (1) and the combustion furnace (2).

摘要翻译： 气化系统具有用于气化废物以产生可燃气体的气化炉（1）和用于燃烧气化炉（1）中气化产生的焦炭和/或焦油的燃烧炉（2）。 气化系统还具有用于将从燃烧炉（2）排出的燃烧气体返回到气化炉（1）和燃烧炉（2）的回流管线。

公开(公告)号：US20060000143A1

公开(公告)日：2006-01-05

申请号：US11210798

申请日：2005-08-25

申请人： Shuichi Nagato ,  Takahiro Oshita ,  Norihisa Miyoshi ,  Seiichiro Toyoda ,  Shugo Hosoda ,  Nobutaka Kashima ,  Katsutoshi Naruse

发明人： Shuichi Nagato ,  Takahiro Oshita ,  Norihisa Miyoshi ,  Seiichiro Toyoda ,  Shugo Hosoda ,  Nobutaka Kashima ,  Katsutoshi Naruse

IPC分类号： C01B3/24

CPC分类号： C10J3/721 ,  C10J3/463 ,  C10J3/86 ,  C10J2200/09 ,  C10J2200/158 ,  C10J2300/093 ,  C10J2300/1637 ,  C10J2300/165 ,  C10J2300/1884 ,  C10J2300/1892 ,  C10K3/003 ,  F17C11/007 ,  Y02P20/124

摘要： A gasification furnace and a combustion furnace are integrated with each other to form a single fluidized-bed gasification and combustion furnace in which unburned char generated in the gasification furnace is combusted in the combustion furnace, and the thus generated heat of combustion is utilized as a heat source for gasification. The fluidized-bed gasification and combustion furnace (1) comprises a gasification furnace (3) and a combustion furnace (4) which are divided by a first partition wall (2). In the gasification furnace (3), a revolving flow of the fluidized medium is formed by diffusion devices (32, 33) provided on furnace bottoms, and an upward flow of the fluidized medium partly flows in the combustion furnace (4). The combustion furnace (4) is divided into a main partition wall (5). In the main combustion chamber (6), a revolving flow of the fluidized medium is formed by diffusion devices (34, 35) provided on furnace bottoms, and an upward flow of the fluidized medium partly flows in the heat recovery chamber (7).

摘要翻译： 气化炉和燃烧炉相互结合形成单一的流化床气化和燃烧炉，其中气化炉中产生的未燃烧焦炭在燃烧炉中燃烧，因此产生的燃烧热被用作 用于气化的热源。 流化床气化和燃烧炉（1）包括由第一分隔壁（2）分隔的气化炉（3）和燃烧炉（4）。 在气化炉（3）中，通过设置在炉底上的扩散装置（32,33）形成流化介质的旋转流，流化介质的向上流动部分地流入燃烧炉（4）。 燃烧炉（4）分为主分隔壁（5）。 在主燃烧室（6）中，通过设置在炉底的扩散装置（34,35）形成流化介质的旋转流，流化介质的向上流动部分地流入热回收室（7）。

公开(公告)号：US20050144844A1

公开(公告)日：2005-07-07

申请号：US11073688

申请日：2005-03-08

申请人： Norihisa Miyoshi ,  Seiichiro Toyoda ,  Shugo Hosoda ,  Nobutaka Kashima ,  Katsutoshi Naruse ,  Katsuyuki Aoki ,  Shinji Sekikawa ,  Shuichi Nagato ,  Hiroshi Hashimoto

发明人： Norihisa Miyoshi ,  Seiichiro Toyoda ,  Shugo Hosoda ,  Nobutaka Kashima ,  Katsutoshi Naruse ,  Katsuyuki Aoki ,  Shinji Sekikawa ,  Shuichi Nagato ,  Hiroshi Hashimoto

IPC分类号： C10J3/54 ,  C10J3/56 ,  C10B1/00

CPC分类号： C10J3/482 ,  C10J3/54 ,  C10J3/56 ,  C10J2300/0916 ,  C10J2300/0946 ,  C10J2300/095 ,  C10J2300/0956 ,  C10J2300/0996 ,  C10J2300/1215 ,  C10J2300/1628 ,  C10J2300/1634 ,  C10J2300/1637 ,  C10J2300/165 ,  C10J2300/1675 ,  C10J2300/1687 ,  C10J2300/1876 ,  C10J2300/1892 ,  F23G5/0276 ,  F23G5/16 ,  F23G5/30 ,  F23G2201/303 ,  F23G2201/304 ,  F23G2201/40 ,  F23G2202/30 ,  F23G2203/502 ,  F23G2206/202 ,  Y02E20/18 ,  Y02P20/124 ,  Y02P20/129

摘要： The present invention provides a fuel gasification furnace including a gasification chamber (1) for fluidizing a high-temperature fluidizing medium therein to form a gasification chamber fluidized bed having an interface, and for gasifying a fuel in the gasification chamber fluidized bed, a char combustion chamber (2) for fluidizing a high-temperature fluidizing medium therein to form a char combustion chamber fluidized bed having an interface, and for combusting char generated by gasification in the gasification chamber (1) in the char combustion chamber fluidized bed to heat the fluidizing medium, and a first energy recovery device (109) for using gases generated by the gasification chamber (1) as a fuel. The gasification chamber (1) and the char combustion chamber (2) are integrated with each other. The gasification chamber (1) and the char combustion chamber (2) are divided from each other by a first partition wall (15) for preventing gases from flowing therebetween, and which extends vertically upward from the interfaces of the respective fluidized beds. The first partition wall (15) has a first opening (25) provided in a lower portion thereof, and the first opening (25) serves as a communication between the gasification chamber (1) and the char combustion chamber (2), for allowing the fluidizing medium heated in the char combustion chamber (2) to move from the char combustion chamber (2) via the first opening (25) into the gasification chamber (1).

摘要翻译： 本发明提供了一种燃料气化炉，其包括用于使其中的高温流化介质流化的气化室（1），以形成具有界面的气化室流化床，并且用于气化气化室流化床中的燃料，焦炭燃烧 用于使其中的高温流化介质流化以形成具有界面的焦炭燃烧室流化床的腔室（2），并且用于在焦炭燃烧室流化床中的气化室（1）中燃烧由气化产生的焦炭，以加热流化 介质和用于使用由气化室（1）产生的气体作为燃料的第一能量回收装置（109）。 气化室（1）和焦炭燃烧室（2）彼此一体化。 气化室（1）和焦炭燃烧室（2）通过第一分隔壁（15）彼此分开，用于防止气体在其间流动，并且从各流化床的界面垂直向上延伸。 第一分隔壁（15）具有设置在其下部的第一开口（25），第一开口（25）用作气化室（1）和焦炭燃烧室（2）之间的连通，以允许 在焦炭燃烧室（2）中加热的流化介质经由第一开口（25）从焦炭燃烧室（2）移动到气化室（1）中。

公开(公告)号：US06350288B1

公开(公告)日：2002-02-26

申请号：US09193127

申请日：1998-11-17

申请人： Yoshio Hirayama ,  Takahiro Oshita ,  Chikashi Tame ,  Shuichi Nagato ,  Tetsuhisa Hirose ,  Norihisa Miyoshi ,  Seiichiro Toyoda ,  Shugo Hosoda ,  Shosaku Fujinami ,  Kazuo Takano

发明人： Yoshio Hirayama ,  Takahiro Oshita ,  Chikashi Tame ,  Shuichi Nagato ,  Tetsuhisa Hirose ,  Norihisa Miyoshi ,  Seiichiro Toyoda ,  Shugo Hosoda ,  Shosaku Fujinami ,  Kazuo Takano

IPC分类号： C10J300

CPC分类号： C10J3/723 ,  C10G2300/1003 ,  C10J3/503 ,  C10J3/523 ,  C10J3/54 ,  C10J3/56 ,  C10J3/64 ,  C10J3/66 ,  C10J3/86 ,  C10J2200/09 ,  C10J2200/158 ,  C10J2300/0946 ,  C10J2300/0956 ,  C10J2300/0959 ,  C10J2300/0973 ,  C10J2300/0983 ,  C10J2300/1628 ,  C10J2300/1634 ,  C10J2300/1637 ,  C10J2300/165 ,  C10J2300/1675 ,  C10J2300/1687 ,  C10J2300/1838 ,  C10J2300/1846 ,  C10J2300/1853 ,  F23G5/006 ,  F23G5/027 ,  F23G5/16 ,  F23G5/30 ,  F23G5/32 ,  F23G2201/40 ,  F23G2202/101 ,  F23G2202/102 ,  F23G2202/103 ,  F23G2202/104 ,  F23G2202/20 ,  F23G2202/30 ,  F23G2203/30 ,  F23G2203/501 ,  F23G2206/00 ,  F23G2206/203 ,  F23G2209/12 ,  F23G2209/20 ,  F23G2209/26 ,  F23G2209/28 ,  F23G2209/281 ,  F23J15/006 ,  F23L7/007 ,  Y02E20/12 ,  Y02E20/16 ,  Y02E20/18 ,  Y02E20/344 ,  Y02P20/129 ,  Y02P20/144

摘要： A combustion method and apparatus in which combustible matter, e.g., waste matter, coal, etc., is gasified to produce a combustible gas containing a sufficiently large amount of combustible component to melt the ash by its own heat. A fluidized-bed furnace (2) has an approximately circular horizontal cross-sectional configuration. A moving bed (9), in which a fluidized medium settles and diffuses, is formed in the central portion of the furnace, and a fluidized bed (10), in which the fluidized medium is actively fluidized, is formed in the peripheral portion in the furnace. The fluidized medium is turned over to the upper part of the moving bed (9) from the upper part of the fluidized bed (10), thus circulating through the two beds. Combustible matter (11) is cast into the upper part of the moving bed (9) and gasified to form a combustible gas while circulating, together with the fluidized medium. The amount of oxygen supplied to the fluidized-bed furnace (2) is set so as to be the same contained in an amount of air not higher than 30% of the theoretical amount of combustion air. The temperature of the fluidized bed (10) is maintained at 450° C. to 650° C. so that the combustible gas produced contains a large amount of combustible component. The combustible gas and fine particles produced in the fluidized-bed furnace (2) are supplied to a melt combustion furnace where they are burned at high temperature, and the resulting ash is melted.

摘要翻译： 燃烧方法和装置，其中将可燃物质，例如废物，煤等气化，以产生含有足够大量可燃组分的可燃气体，以通过其自身的热量来熔化灰分。 流化床炉（2）具有近似圆形的横截面构造。 在炉的中心部分形成有流化介质沉降扩散的移动床（9），流化床主动流化的流化床（10）形成在周边部分 炉子。 流化介质从流化床（10）的上部翻转到移动床（9）的上部，从而循环通过两个床。 将可燃物（11）流入移动床（9）的上部并与流化介质一起循环而气化形成可燃气体。 供给到流化床炉（2）的氧气的量被设定为含有不高于理论量的燃烧空气的30％的空气量。 流化床（10）的温度保持在450℃至650℃，使得产生的可燃气体含有大量的可燃组分。 在流化床炉（2）中生产的可燃气体和细颗粒被供给到熔化炉中，在其中它们在高温下燃烧，并且所得到的灰分熔化。

公开(公告)号：USRE37300E1

公开(公告)日：2001-07-31

申请号：US09073062

申请日：1998-05-06

申请人： Shuichi Nagato ,  Masayuki Horio ,  Takahiro Oshita ,  Norihisa Miyoshi ,  Seiichiro Toyoda ,  Akira Shimokura ,  Tomoyuki Shinano ,  Shugo Hosoda

发明人： Shuichi Nagato ,  Masayuki Horio ,  Takahiro Oshita ,  Norihisa Miyoshi ,  Seiichiro Toyoda ,  Akira Shimokura ,  Tomoyuki Shinano ,  Shugo Hosoda

IPC分类号： B09B300

CPC分类号： C10J3/723 ,  C10J3/463 ,  C10J3/56 ,  C10J3/76 ,  C10J3/86 ,  C10J2200/09 ,  C10J2200/15 ,  C10J2300/0956 ,  C10J2300/1675 ,  C10J2300/1687 ,  F01K23/062 ,  F01K23/067 ,  F22B31/0092 ,  F23C10/06 ,  F23C10/10 ,  F23C10/16 ,  F23C10/20 ,  F23C10/28 ,  F23L7/00 ,  F23L9/04 ,  F23L2900/07005 ,  F23L2900/07009 ,  Y02E20/16 ,  Y02E20/18 ,  Y02E20/344 ,  Y02P20/123 ,  Y02P20/124 ,  Y02P20/129

摘要： A pressurized internal circulating fluidized-bed boiler is incorporated in a combined-cycle electric generating system in which a fuel such as coal, petro coke or the like is combusted in a pressurized fluidized bed and an exhaust gas produced by the combusted fuel is introduced into a gas turbine. The pressurized internal circulating fluidized-bed boiler includes a pressure vessel, a combustor disposed in the pressure vessel and a main fluidized bed combustion chamber provided with an air diffusion device. A thermal energy recovery chamber is partitioned from the main combustion chamber by an inclined partition wall. A fluidized medium flows into and out of the main combustion chamber and the thermal energy recovery chamber. A free board is provided integrally above the main combustion chamber and the thermal energy recovery chamber so that combustion gas from the main combustion chamber and the thermal energy recovery chamber is mixed in the free board.

摘要翻译： 加压的内部循环流化床锅炉被并入到组合循环发电系统中，其中诸如煤，石油焦炭等的燃料在加压流化床中燃烧，并且由燃烧的燃料产生的废气被引入 一个燃气轮机。 加压内循环流化床锅炉包括压力容器，设置在压力容器中的燃烧器和设置有空气扩散装置的主流化床燃烧室。 热能回收室通过倾斜的分隔壁与主燃烧室隔开。 流化介质流入和流出主燃烧室和热能回收室。 在主燃烧室和热能回收室一体地设置有空板，使得来自主燃烧室和热能回收室的燃烧气体在自由板中混合。

公开(公告)号：US5725614A

公开(公告)日：1998-03-10

申请号：US547126

申请日：1995-10-24

申请人： Yoshio Hirayama ,  Takahiro Oshita ,  Chikashi Tame ,  Shuichi Nagato ,  Tetsuhisa Hirose ,  Norihisa Miyoshi ,  Seiichiro Toyoda ,  Shugo Hosoda ,  Shosaku Fujinami ,  Kazuo Takano

发明人： Yoshio Hirayama ,  Takahiro Oshita ,  Chikashi Tame ,  Shuichi Nagato ,  Tetsuhisa Hirose ,  Norihisa Miyoshi ,  Seiichiro Toyoda ,  Shugo Hosoda ,  Shosaku Fujinami ,  Kazuo Takano

IPC分类号： C10J3/46 ,  C10J3/48 ,  C10J3/50 ,  C10J3/52 ,  C10J3/54 ,  C10J3/56 ,  C10J3/64 ,  C10J3/66 ,  C10J3/86 ,  F23C10/00 ,  F23C10/02 ,  F23C10/12 ,  F23G5/00 ,  F23G5/027 ,  F23G5/16 ,  F23G5/30 ,  F23G5/32 ,  F23G5/46 ,  F23J1/00 ,  F23J15/00 ,  F23L7/00 ,  C10J3/68 ,  C10J3/00 ,  F27B15/08

CPC分类号： C10J3/723 ,  C10J3/503 ,  C10J3/523 ,  C10J3/54 ,  C10J3/56 ,  C10J3/64 ,  C10J3/66 ,  C10J3/86 ,  F23G5/006 ,  F23G5/027 ,  F23G5/16 ,  F23G5/30 ,  F23G5/32 ,  F23J15/006 ,  F23L7/007 ,  C10G2300/1003 ,  C10J2200/09 ,  C10J2200/158 ,  C10J2300/0946 ,  C10J2300/0956 ,  C10J2300/0959 ,  C10J2300/0973 ,  C10J2300/0983 ,  C10J2300/1628 ,  C10J2300/1634 ,  C10J2300/1637 ,  C10J2300/165 ,  C10J2300/1675 ,  C10J2300/1687 ,  C10J2300/1838 ,  C10J2300/1846 ,  C10J2300/1853 ,  F23G2201/40 ,  F23G2202/101 ,  F23G2202/102 ,  F23G2202/103 ,  F23G2202/104 ,  F23G2202/20 ,  F23G2202/30 ,  F23G2203/30 ,  F23G2203/501 ,  F23G2206/00 ,  F23G2206/203 ,  F23G2209/12 ,  F23G2209/20 ,  F23G2209/26 ,  F23G2209/28 ,  F23G2209/281 ,  Y02E20/12 ,  Y02E20/16 ,  Y02E20/18 ,  Y02E20/344 ,  Y02P20/129 ,  Y02P20/144

摘要： A combustion apparatus in which combustible matter, e.g., waste matter, coal, etc., is gasified to produce a combustible gas containing a sufficiently large amount of combustible component to melt ash by its own heat. A fluidized-bed furnace has an approximately circular horizontal cross-sectional configuration. A moving bed, in which a fluidized medium settles and diffuses, is formed in the central portion of the furnace, and a fluidized bed, in which the fluidized medium is actively fluidized, is formed in a peripheral portion in the furnace. The fluidized medium is turned over to the upper part of the moving bed from the upper part of the fluidized bed, thus circulating through the two beds. Combustible matter is cast into the upper part of the moving bed and gasified to form a combustible gas while circulating, together with the fluidized medium. The amount of oxygen supplied to the fluidized-bed furnace is set so as to be not higher than 30% of the theoretical amount of oxygen necessary to combust the combustible matter. The temperature of the fluidized bed is maintained at 450.degree. C. to 650.degree. C. so that the combustible gas produced contains a large amount of combustible component.

摘要翻译： 将燃烧物质，例如废物，煤等气化的燃烧装置，以产生含有足够大量的可燃组分的可燃气体，以通过其自身的热量来熔化灰分。 流化床炉具有近似圆形的横截面构造。 在炉的中央部形成有流化介质沉降扩散的移动床，在炉的周边部形成流化床主动流化的流化床。 流化介质从流化床的上部翻转到移动床的上部，从而循环通过两个床。 将可燃物投入到移动床的上部，并与流化介质一起气化以形成可燃气体同时循环。 供给流化床炉的氧气的量设定为不高于燃烧可燃物质所需的理论氧气的30％。 流化床的温度保持在450℃至650℃，使得产生的可燃气体含有大量的可燃组分。

公开(公告)号：US07390337B2

公开(公告)日：2008-06-24

申请号：US11073688

申请日：2005-03-08

申请人： Norihisa Miyoshi ,  Seiichiro Toyoda ,  Shugo Hosoda ,  Nobutaka Kashima ,  Katsutoshi Naruse ,  Katsuyuki Aoki ,  Shinji Sekikawa ,  Shuichi Nagato ,  Hiroshi Hashimoto

发明人： Norihisa Miyoshi ,  Seiichiro Toyoda ,  Shugo Hosoda ,  Nobutaka Kashima ,  Katsutoshi Naruse ,  Katsuyuki Aoki ,  Shinji Sekikawa ,  Shuichi Nagato ,  Hiroshi Hashimoto

IPC分类号： B01J8/00 ,  B01J8/18

CPC分类号： C10J3/482 ,  C10J3/54 ,  C10J3/56 ,  C10J2300/0916 ,  C10J2300/0946 ,  C10J2300/095 ,  C10J2300/0956 ,  C10J2300/0996 ,  C10J2300/1215 ,  C10J2300/1628 ,  C10J2300/1634 ,  C10J2300/1637 ,  C10J2300/165 ,  C10J2300/1675 ,  C10J2300/1687 ,  C10J2300/1876 ,  C10J2300/1892 ,  F23G5/0276 ,  F23G5/16 ,  F23G5/30 ,  F23G2201/303 ,  F23G2201/304 ,  F23G2201/40 ,  F23G2202/30 ,  F23G2203/502 ,  F23G2206/202 ,  Y02E20/18 ,  Y02P20/124 ,  Y02P20/129

摘要： The present invention provides a fuel gasification furnace including a gasification chamber (1) for fluidizing a high-temperature fluidizing medium therein to form a gasification chamber fluidized bed having an interface, and for gasifying a fuel in the gasification chamber fluidized bed, a char combustion chamber (2) for fluidizing a high-temperature fluidizing medium therein to form a char combustion chamber fluidized bed having an interface, and for combusting char generated by gasification in the gasification chamber (1) in the char combustion chamber fluidized bed to heat the fluidizing medium, and a first energy recovery device (109) for using gases generated by the gasification chamber (1) as a fuel. The gasification chamber (1) and the char combustion chamber (2) are integrated with each other. The gasification chamber (1) and the char combustion chamber (2) are divided from each other by a first partition wall (15) for preventing gases from flowing therebetween, and which extends vertically upward from the interfaces of the respective fluidized beds. The first partition wall (15) has a first opening (25) provided in a lower portion thereof, and the first opening (25) serves as a communication between the gasification chamber (1) and the char combustion chamber (2), for allowing the fluidizing medium heated in the char combustion chamber (2) to move from the char combustion chamber (2) via the first opening (25) into the gasification chamber (1).

公开(公告)号：US5858033A

公开(公告)日：1999-01-12

申请号：US915322

申请日：1997-08-20

申请人： Yoshio Hirayama ,  Takahiro Oshita ,  Chikashi Tame ,  Shuichi Nagato ,  Tetsuhisa Hirose ,  Norihisa Miyoshi ,  Seiichiro Toyoda ,  Shugo Hosoda ,  Shosaku Fujinami ,  Kazuo Takano

发明人： Yoshio Hirayama ,  Takahiro Oshita ,  Chikashi Tame ,  Shuichi Nagato ,  Tetsuhisa Hirose ,  Norihisa Miyoshi ,  Seiichiro Toyoda ,  Shugo Hosoda ,  Shosaku Fujinami ,  Kazuo Takano

IPC分类号： C10J3/46 ,  C10J3/48 ,  C10J3/50 ,  C10J3/52 ,  C10J3/54 ,  C10J3/56 ,  C10J3/64 ,  C10J3/66 ,  C10J3/86 ,  F23C10/00 ,  F23C10/02 ,  F23C10/12 ,  F23G5/00 ,  F23G5/027 ,  F23G5/16 ,  F23G5/30 ,  F23G5/32 ,  F23G5/46 ,  F23J1/00 ,  F23J15/00 ,  F23L7/00 ,  C01B3/32 ,  F23J11/00 ,  F27B15/14

CPC分类号： C10J3/723 ,  C10J3/503 ,  C10J3/523 ,  C10J3/54 ,  C10J3/56 ,  C10J3/64 ,  C10J3/66 ,  C10J3/86 ,  F23G5/006 ,  F23G5/027 ,  F23G5/16 ,  F23G5/30 ,  F23G5/32 ,  F23J15/006 ,  F23L7/007 ,  C10G2300/1003 ,  C10J2200/09 ,  C10J2200/158 ,  C10J2300/0946 ,  C10J2300/0956 ,  C10J2300/0959 ,  C10J2300/0973 ,  C10J2300/0983 ,  C10J2300/1628 ,  C10J2300/1634 ,  C10J2300/1637 ,  C10J2300/165 ,  C10J2300/1675 ,  C10J2300/1687 ,  C10J2300/1838 ,  C10J2300/1846 ,  C10J2300/1853 ,  F23G2201/40 ,  F23G2202/101 ,  F23G2202/102 ,  F23G2202/103 ,  F23G2202/104 ,  F23G2202/20 ,  F23G2202/30 ,  F23G2203/30 ,  F23G2203/501 ,  F23G2206/00 ,  F23G2206/203 ,  F23G2209/12 ,  F23G2209/20 ,  F23G2209/26 ,  F23G2209/28 ,  F23G2209/281 ,  Y02E20/12 ,  Y02E20/16 ,  Y02E20/18 ,  Y02E20/344 ,  Y02P20/129 ,  Y02P20/144

摘要： A combustion method and apparatus in which combustible matter, e.g., waste matter, coal, etc., is gasified to produce a combustible gas containing a sufficiently large amount of combustible component to melt ash by its own heat. A fluidized-bed furnace has an approximately circular horizontal cross-sectional configuration. A moving bed, in which a fluidized medium settles and diffuses, is formed in the central portion of the furnace, and a fluidized bed, in which the fluidized medium is actively fluidized, is formed in the peripheral portion in the furnace. The fluidized medium is turned over to the upper part of the moving bed from the upper part of the fluidized bed, thus circulating through the two beds. Combustible matter is cast into the upper part of the moving bed and gasified to form a combustible gas while circulating, together with the fluidized medium. The amount of oxygen supplied to the fluidized-bed furnace is set so as to be not higher than 30% of the theoretical amount of oxygen required for combustion. The temperature of the fluidized bed is maintained at 450.degree. C. to 650.degree. C. so that the combustible gas produced contains a large amount of combustible component. The combustible gas and fine particles produced in the fluidized-bed furnace are supplied to a melt combustion furnace where they are burned at high temperature, and the resulting ash is melted.

摘要翻译： 燃烧方法和装置，其中可燃物质例如废物，煤等被气化以产生含有足够大量的可燃组分的可燃气体，以通过其自身的热量来熔化灰分。 流化床炉具有近似圆形的横截面构造。 在炉的中央部形成有流化介质沉降扩散的移动床，在炉的周边部形成流化床主动流化的流化床。 流化介质从流化床的上部翻转到移动床的上部，从而循环通过两个床。 将可燃物投入到移动床的上部，并与流化介质一起气化以形成可燃气体同时循环。 供给到流化床炉的氧量设定为不高于燃烧所需的理论氧量的30％。 流化床的温度保持在450℃至650℃，使得产生的可燃气体含有大量的可燃组分。 在流化床炉中产生的可燃性气体和细颗粒被供给到熔融燃烧炉中，在高温下燃烧，并使所得灰分熔化。

公开(公告)号：US5620488A

公开(公告)日：1997-04-15

申请号：US401370

申请日：1995-03-09

申请人： Yoshio Hirayama ,  Takahiro Oshita ,  Chikashi Tame ,  Shuichi Nagato ,  Tetsuhisa Hirose ,  Norihisa Miyoshi ,  Seiichiro Toyoda ,  Shugo Hosoda ,  Shosaku Fujinami ,  Kazuo Takano

发明人： Yoshio Hirayama ,  Takahiro Oshita ,  Chikashi Tame ,  Shuichi Nagato ,  Tetsuhisa Hirose ,  Norihisa Miyoshi ,  Seiichiro Toyoda ,  Shugo Hosoda ,  Shosaku Fujinami ,  Kazuo Takano

IPC分类号： C10J3/46 ,  C10J3/48 ,  C10J3/50 ,  C10J3/52 ,  C10J3/54 ,  C10J3/56 ,  C10J3/64 ,  C10J3/66 ,  C10J3/86 ,  F23C10/00 ,  F23C10/02 ,  F23C10/12 ,  F23G5/00 ,  F23G5/027 ,  F23G5/16 ,  F23G5/30 ,  F23G5/32 ,  F23G5/46 ,  F23J1/00 ,  F23J15/00 ,  F23L7/00 ,  B09B3/00 ,  F22B1/00 ,  F27B15/16

CPC分类号： C10J3/723 ,  C10J3/503 ,  C10J3/523 ,  C10J3/54 ,  C10J3/56 ,  C10J3/64 ,  C10J3/66 ,  C10J3/86 ,  F23G5/006 ,  F23G5/027 ,  F23G5/16 ,  F23G5/30 ,  F23G5/32 ,  F23J15/006 ,  F23L7/007 ,  C10G2300/1003 ,  C10J2200/09 ,  C10J2200/158 ,  C10J2300/0946 ,  C10J2300/0956 ,  C10J2300/0959 ,  C10J2300/0973 ,  C10J2300/0983 ,  C10J2300/1628 ,  C10J2300/1634 ,  C10J2300/1637 ,  C10J2300/165 ,  C10J2300/1675 ,  C10J2300/1687 ,  C10J2300/1838 ,  C10J2300/1846 ,  C10J2300/1853 ,  F23G2201/40 ,  F23G2202/101 ,  F23G2202/102 ,  F23G2202/103 ,  F23G2202/104 ,  F23G2202/20 ,  F23G2202/30 ,  F23G2203/30 ,  F23G2203/501 ,  F23G2206/00 ,  F23G2206/203 ,  F23G2209/12 ,  F23G2209/20 ,  F23G2209/26 ,  F23G2209/28 ,  F23G2209/281 ,  Y02E20/12 ,  Y02E20/16 ,  Y02E20/18 ,  Y02E20/344 ,  Y02P20/129 ,  Y02P20/144

摘要： A combustion method and apparatus in which combustible matter, e.g., waste matter, coal, etc., is gasified to produce a combustible gas containing a sufficiently large amount of combustible component to melt ash by its own heat. A fluidized-bed furnace has an approximately circular horizontal cross-sectional configuration. A moving bed, in which a fluidized medium settles and diffuses, is formed in a central portion of the furnace, and a fluidized bed, in which the fluidized medium is actively fluidized, is formed in a peripheral portion in the furnace. The fluidized medium is turned over to the upper part of the moving bed from the upper part of the fluidized bed, thus circulating through the two beds. Combustible matter is cast into the upper part of the moving bed and gasified to form a combustible gas while circulating, together with the fluidized medium. The amount of oxygen supplied to the fluidized-bed furnace is set so as to be not higher than 30% of the theoretical amount of oxygen necessary to combust the combustible matter. The temperature of the fluidized bed is maintained at 450.degree. C. to 650.degree. C. so that the combustible gas produced contains a large amount of combustible component. The combustible gas and fine particles produced in the fluidized-bed furnace are supplied to a melt combustion furnace where they are burned at high temperature, and the resulting ash is melted.

摘要翻译： 燃烧方法和装置，其中可燃物质例如废物，煤等被气化以产生含有足够大量的可燃组分的可燃气体，以通过其自身的热量来熔化灰分。 流化床炉具有近似圆形的横截面构造。 在炉的中心部分形成流化介质沉降扩散的移动床，在炉的周边部分形成流化床主动流化的流化床。 流化介质从流化床的上部翻转到移动床的上部，从而循环通过两个床。 将可燃物投入到移动床的上部，并与流化介质一起气化以形成可燃气体同时循环。 供给流化床炉的氧气的量设定为不高于燃烧可燃物质所需的理论氧气的30％。 流化床的温度保持在450℃至650℃，使得产生的可燃气体含有大量的可燃组分。 在流化床炉中产生的可燃性气体和细颗粒被供给到熔融燃烧炉中，在高温下燃烧，并使所得灰分熔化。