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。

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：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。