公开(公告)号：US08500443B2

公开(公告)日：2013-08-06

申请号：US12934546

申请日：2009-03-11

申请人： Tomoyuki Katagiri ,  Hisanori Nukumi ,  Kenichiro Kondo

发明人： Tomoyuki Katagiri ,  Hisanori Nukumi ,  Kenichiro Kondo

IPC分类号： F27B15/10

CPC分类号： C10J3/463 ,  C10J3/728 ,  C10J2300/0976 ,  C10J2300/0993 ,  C10J2300/1637 ,  C10J2300/1807 ,  F23G5/0276 ,  F23G5/30 ,  F23G2201/304 ,  F23G2201/40 ,  F23G2203/501 ,  F23G2203/503 ,  F23G2208/10

摘要： A fluidized bed gasification furnace has a fluidized bed formed and a freeboard section F above a bed material so as to produce a produced gas by a reaction of raw material with a gasifying agent and take out the produced gas through the freeboard section. Upon shutdown of the furnace, inert gas is fed from below to the furnace for purging of gas in the fluidized bed with inert gas while steam is supplied to a freeboard section above the fluidized bed to purge a gas in the freeboard section with steam.

摘要翻译： 流化床气化炉具有形成的流化床和在床材料上方的干舷部分F，以便通过原料与气化剂的反应产生产生的气体，并通过干舷段取出产生的气体。 关闭炉后，将惰性气体从下方进料到炉中，用惰性气体吹送流化床中的气体，同时将蒸汽供应到流化床上方的干舷部分，以用蒸汽吹扫干舷段中的气体。

公开(公告)号：US20110020145A1

公开(公告)日：2011-01-27

申请号：US12934546

申请日：2009-03-11

申请人： Tomoyuki Katagiri ,  Hisanori Nukumi ,  Kenichiro Kondo

发明人： Tomoyuki Katagiri ,  Hisanori Nukumi ,  Kenichiro Kondo

IPC分类号： F04F5/44

CPC分类号： C10J3/463 ,  C10J3/728 ,  C10J2300/0976 ,  C10J2300/0993 ,  C10J2300/1637 ,  C10J2300/1807 ,  F23G5/0276 ,  F23G5/30 ,  F23G2201/304 ,  F23G2201/40 ,  F23G2203/501 ,  F23G2203/503 ,  F23G2208/10

摘要： A fluidized bed gasification furnace has a fluidized bed formed and a freeboard section F above a bed material so as to produce a produced gas by a reaction of raw material with a gasifying agent and take out the produced gas through the freeboard section. Upon shutdown of the furnace, inert gas is fed from below to the furnace for purging of gas in the fluidized bed with inert gas while steam is supplied to a freeboard section above the fluidized bed to purge a gas in the freeboard section with steam.

摘要翻译： 流化床气化炉具有形成的流化床和在床材料上方的干舷部分F，以便通过原料与气化剂的反应产生产生的气体，并通过干舷段取出产生的气体。 关闭炉后，将惰性气体从下方进料到炉中，用惰性气体吹送流化床中的气体，同时将蒸汽供应到流化床上方的干舷部分，以用蒸汽吹扫干舷段中的气体。

公开(公告)号：US08425638B2

公开(公告)日：2013-04-23

申请号：US12933545

申请日：2009-03-18

申请人： Hisanori Nukumi ,  Tomoyuki Katagiri

发明人： Hisanori Nukumi ,  Tomoyuki Katagiri

IPC分类号： C01B3/36 ,  C01B6/24 ,  C10J3/00 ,  C10J1/207 ,  B01J7/00

CPC分类号： C10J3/463 ,  C10J2300/093 ,  C10J2300/0956 ,  C10J2300/0976 ,  C10J2300/0993 ,  C10J2300/1637 ,  C10J2300/1807 ,  F23G5/0276 ,  F23G5/30 ,  F23G5/50 ,  F23G7/12 ,  F23G2201/304 ,  F23G2201/40 ,  F23G2203/501 ,  F23G2203/503 ,  F23G2209/281 ,  Y02E20/18 ,  Y02P20/124 ,  Y02P20/129

摘要： Upon cold startup of a gasification facility, a fluidized air 10 is supplied to a combustion furnace 9 to fluidize a combustion-furnace fluidized bed 11 while a preheating fuel 22 is supplied to the combustion furnace to preheat the fluidized bed 11 up to an autoignition temperature of coal. Then, a coal 23 is charged to the combustion furnace 9 to heat the fluidized bed 11 and bed material is circulated between the combustion and gasification furnaces 9 and 1 for heating. Upon startup and shutdown of the gasification facility, steam 2 from an exhaust heat recovery boiler 20 in heat exchange with an exhaust gas 15 from the combustion furnace 9 is supplied to the gasification furnace 1 to purge the gasification furnace 1 and a lead-out passage 6 with the steam 2 utilizing the exhaust heat.

摘要翻译： 在气化设备冷启动时，将流化空气10供应到燃烧炉9以使燃烧炉流化床11流化，同时向燃烧炉供应预热燃料22以将流化床11预热至自燃温度 的煤。 然后，将煤23装入燃烧炉9以加热流化床11，并使床料在燃烧炉和气化炉9和1之间循环进行加热。 在气化设备启动和关闭时，将来自与来自燃烧炉9的废气15热交换的废热回收锅炉20的蒸汽2供给到气化炉1，以吹扫气化炉1和引出通道 6，蒸汽2利用废热。

公开(公告)号：US20110016789A1

公开(公告)日：2011-01-27

申请号：US12933545

申请日：2009-03-18

申请人： Hisanori Nukumi ,  Tomoyuki Katagiri

发明人： Hisanori Nukumi ,  Tomoyuki Katagiri

IPC分类号： C10J3/48

CPC分类号： C10J3/463 ,  C10J2300/093 ,  C10J2300/0956 ,  C10J2300/0976 ,  C10J2300/0993 ,  C10J2300/1637 ,  C10J2300/1807 ,  F23G5/0276 ,  F23G5/30 ,  F23G5/50 ,  F23G7/12 ,  F23G2201/304 ,  F23G2201/40 ,  F23G2203/501 ,  F23G2203/503 ,  F23G2209/281 ,  Y02E20/18 ,  Y02P20/124 ,  Y02P20/129

摘要： Upon cold startup of a gasification facility, a fluidized air 10 is supplied to a combustion furnace 9 to fluidize a combustion-furnace fluidized bed 11 while a preheating fuel 22 is supplied to the combustion furnace to preheat the fluidized bed 11 up to an autoignition temperature of coal. Then, a coal 23 is charged to the combustion furnace 9 to heat the fluidized bed 11 and bed material is circulated between the combustion and gasification furnaces 9 and 1 for heating. Upon startup and shutdown of the gasification facility, steam 2 from an exhaust heat recovery boiler 20 in heat exchange with an exhaust gas 15 from the combustion furnace 9 is supplied to the gasification furnace 1 to purge the gasification furnace 1 and a lead-out passage 6 with the steam 2 utilizing the exhaust heat.

摘要翻译： 在气化设备冷启动时，将流化空气10供应到燃烧炉9以使燃烧炉流化床11流化，同时向燃烧炉供应预热燃料22以将流化床11预热至自燃温度 的煤。 然后，将煤23装入燃烧炉9以加热流化床11，并使床料在燃烧炉和气化炉9和1之间循环进行加热。 在气化设备启动和关闭时，将来自与来自燃烧炉9的废气15热交换的废热回收锅炉20的蒸汽2供给到气化炉1，以吹扫气化炉1和引出通道 6，蒸汽2利用废热。

公开(公告)号：US08545579B2

公开(公告)日：2013-10-01

申请号：US12921802

申请日：2009-03-18

申请人： Hisanori Nukumi ,  Toshiyuki Suda ,  Tomoya Muramoto

发明人： Hisanori Nukumi ,  Toshiyuki Suda ,  Tomoya Muramoto

IPC分类号： B01J7/00 ,  B01J8/18 ,  C10B1/00

CPC分类号： C10J3/482 ,  C10J2300/0916 ,  C10J2300/093 ,  C10J2300/0946 ,  C10J2300/0976 ,  C10J2300/0993 ,  C10J2300/1637 ,  C10J2300/1807 ,  C10J2300/1853 ,  C10K1/026 ,  F23G5/0276 ,  F23G5/30 ,  F23G7/12 ,  F23G2201/304 ,  F23G2201/40 ,  F23G2203/501 ,  F23G2203/503 ,  F23G2209/281

摘要： A gasification furnace 2 is divided into a plurality of gasification furnace units 2a and 2b each of which has an inlet 15a, 15b on a lower portion at a longitudinally upstream end in a direction of travel of raw and bed materials and has an outlet 16a, 16b on an upper portion at a longitudinally downstream end in the direction of travel. The outlet 16a is connected to the inlet 15b. The inlet 15a is fed with a raw material and a hot bed material from a materials separator 8. The inlet 15b is also fed with the hot bed material from the material separator 8. The outlet 16b is connected to a combustion furnace 5.

摘要翻译： 气化炉2分为多个气化炉单元2a和2b，每个气化炉单元2a和2b在原料和床料的行进方向上的纵向上游端的下部具有入口15a，15b，并具有出口16a， 16b在行进方向上的纵向下游端的上部。 出口16a连接到入口15b。 入口15a从材料分离器8供给原料和热床材料。入口15b还从材料分离器8送入热床材料。出口16b连接到燃烧炉5。

公开(公告)号：US20110027132A1

公开(公告)日：2011-02-03

申请号：US12921802

申请日：2009-03-18

申请人： Hisanori Nukumi ,  Toshiyuki Suda ,  Tomoya Muramoto

发明人： Hisanori Nukumi ,  Toshiyuki Suda ,  Tomoya Muramoto

IPC分类号： F27B15/14

CPC分类号： C10J3/482 ,  C10J2300/0916 ,  C10J2300/093 ,  C10J2300/0946 ,  C10J2300/0976 ,  C10J2300/0993 ,  C10J2300/1637 ,  C10J2300/1807 ,  C10J2300/1853 ,  C10K1/026 ,  F23G5/0276 ,  F23G5/30 ,  F23G7/12 ,  F23G2201/304 ,  F23G2201/40 ,  F23G2203/501 ,  F23G2203/503 ,  F23G2209/281

摘要： A gasification furnace 2 is divided into a plurality of gasification furnace units 2a and 2b each of which has an inlet 15a, 15b on a lower portion at a longitudinally upstream end in a direction of travel of raw and bed materials and has an outlet 16a, 16b on an upper portion at a longitudinally downstream end in the direction of travel. The outlet 16a is connected to the inlet 15b. The inlet 15a is fed with a raw material and a hot bed material from a materials separator 8. The inlet 15b is also fed with the hot bed material from the material separator 8. The outlet 16b is connected to a combustion furnace 5.

摘要翻译： 气化炉2分为多个气化炉单元2a和2b，每个气化炉单元2a和2b在原料和床料的行进方向上的纵向上游端的下部具有入口15a，15b，并具有出口16a， 16b在行进方向上的纵向下游端的上部。 出口16a连接到入口15b。 入口15a从材料分离器8供给原料和热床材料。入口15b还从材料分离器8送入热床材料。出口16b连接到燃烧炉5。