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    METHOD FOR PROCESSING SPODUMENE
    1.
    发明申请
    METHOD FOR PROCESSING SPODUMENE 有权
    处理泡沫的方法

    公开(公告)号：US20130042438A1

    公开(公告)日：2013-02-21

    申请号：US13643502

    申请日：2011-05-12

    申请人： Maija-Leena Metsärinta

    发明人： Maija-Leena Metsärinta

    IPC分类号： C09C1/40

    CPC分类号： C22B1/00 ,  C22B1/10 ,  C22B26/12 ,  F23C10/005 ,  F23C10/10 ,  F23C10/28 ,  F23C2206/103 ,  F23C2900/10001 ,  F23L2900/07006 ,  Y02E20/344

    摘要： The invention relates to a method for thermally processing α-spodumene, i.e. lithium aluminum silicate, by which treatment it is transformed into β-spodumene, which is more advantageous for further processing; in the method, concentrate or ore with a grain size of 20-1,000 μm is processed in a fluidized bed reactor, at a temperature of 800-1,000° C., by using an oxygenous gas as the fluidizing gas.

    摘要翻译： 本发明涉及一种用于热处理α-锂辉石（即，硅酸铝锂）的方法，通过该方法将其转化为“泡”，其对于进一步加工更有利; 在该方法中，通过使用氧气作为流化气体，在流化床反应器中，在800-1,000℃的温度下处理粒径为20-1,000μm的浓缩物或矿石。

    Method for energy conversion minimizing oxygen consumption
    2.
    发明授权
    Method for energy conversion minimizing oxygen consumption 有权
    能量转换方法最大限度地减少氧气消耗

    公开(公告)号：US07820139B2

    公开(公告)日：2010-10-26

    申请号：US11628928

    申请日：2005-06-09

    申请人： Jean-Xavier Morin ,  Corinne Beal

    发明人： Jean-Xavier Morin ,  Corinne Beal

    IPC分类号： C01B3/26 ,  C01B3/24

    CPC分类号： F23C10/005 ,  C10J3/56 ,  C10J2300/0916 ,  C10J2300/0969 ,  C10J2300/0973 ,  C10J2300/0983 ,  F23C10/10 ,  F23C2900/03002 ,  F23C2900/10001 ,  F23C2900/10005 ,  F23C2900/99008 ,  Y02E20/346

    摘要： The invention concerns a method for energy conversion of solid fuels in particular containing carbon comprising a first step which consists in reacting said fuels in a first energy conversion reactor (2, 20). The invention is characterized in that it comprises a second step which consists in injecting oxygen brought to the output of said reactor (2, 20), the reaction of the first step being carried out in at least a circulating fluidized bed (30, 31, 40) and in that the metal oxides circulate between two interconnected circulating fluidized beds (30, 31, 40) converting the fuel and oxidizing the oxides.

    摘要翻译： 本发明涉及一种固体燃料特别是含有碳的能量转化的方法，其包括第一步骤，该第一步骤包括在第一能量转换反应器（2,20）中使所述燃料反应。 本发明的特征在于，其包括第二步骤，其中包括将产生的氧气注入所述反应器（2,20）的输出，所述第一步骤的反应在至少循环流化床（30,31， 并且金属氧化物在两个相互连接的循环流化床（30,31,40）之间循环，转化燃料并氧化氧化物。

    Circulating fluidized bed gasification furnace
    7.
    发明授权
    Circulating fluidized bed gasification furnace 有权
    循环流化床气化炉

    公开(公告)号：US08864856B2

    公开(公告)日：2014-10-21

    申请号：US13003413

    申请日：2009-07-10

    申请人： Makoto Takafuji ,  Toshiyuki Suda

    发明人： Makoto Takafuji ,  Toshiyuki Suda

    IPC分类号： B01J7/00 ,  F23C10/26 ,  F23C10/32 ,  C10J3/46 ,  F23C10/10

    CPC分类号： F23C10/10 ,  C10J3/463 ,  C10J2300/0993 ,  C10J2300/1637 ,  C10J2300/1807 ,  F23C10/26 ,  F23C10/32 ,  F23C2900/10001

    摘要： A circulating fluidized bed gasification furnace has a combustion furnace 1, a cyclone collector 4 to which a combustion exhaust gas 3 from the combustion furnace 1 is introduced to collect a circulating medium 5, a fluidized bed gasification furnace 8 for formation of a fluidized bed 10 by introducing the circulating medium 5 collected in the cyclone collector 4 through a downcomer 7 and by supplying a gasification agent 9 from below and for gasification of a raw material 12 by supplying the same to a freeboard 11, and a circulation flow passage 14 for return of the circulating medium and unreacted char not gasified in the gasification furnace 8 to the combustion furnace 1. The downcomer 7 connected to the collector 4 has a lower end connected through a sealer 18 to the freeboard 11 in the gasification furnace 8. A raw material supply unit 20 is arranged to supply the raw material 12 to the circulating medium 5 between the sealer 18 and the freeboard 11.

    摘要翻译： 循环流化床气化炉具有燃烧炉1，将来自燃烧炉1的燃烧废气3引入其中以收集循环介质5的旋风收集器4，用于形成流化床10的流化床气化炉8 通过下降管7引入收集在旋风收集器4中的循环介质5，并从下方供给气化剂9，并通过将原料12供给到干舷11进行气化，以及循环流路14返回 循环介质和未反应的焦炭未在气化炉8中气化到燃烧炉1中。连接到集电器4的降液管7的下端通过密封件18连接到气化炉8中的干舷11。 供给单元20被布置成将原料12供给到密封件18和干舷11之间的循环介质5。

    CIRCULATING FLUIDIZED BED GASIFICATION FURNACE
    8.
    发明申请
    CIRCULATING FLUIDIZED BED GASIFICATION FURNACE 有权
    循环流化床气化炉

    公开(公告)号：US20110104014A1

    公开(公告)日：2011-05-05

    申请号：US13003413

    申请日：2009-07-10

    申请人： Makoto Takafuji ,  Toshiyuki Suda

    发明人： Makoto Takafuji ,  Toshiyuki Suda

    IPC分类号： B01J8/18

    CPC分类号： F23C10/10 ,  C10J3/463 ,  C10J2300/0993 ,  C10J2300/1637 ,  C10J2300/1807 ,  F23C10/26 ,  F23C10/32 ,  F23C2900/10001

    摘要： A circulating fluidized bed gasification furnace has a combustion furnace 1, a cyclone collector 4 to which a combustion exhaust gas 3 from the combustion furnace 1 is introduced to collect a circulating medium 5, a fluidized bed gasification furnace 8 for formation of a fluidized bed 10 by introducing the circulating medium 5 collected in the cyclone collector 4 through a downcomer 7 and by supplying a gasification agent 9 from below and for gasification of a raw material 12 by supplying the same to a freeboard 11, and a circulation flow passage 14 for return of the circulating medium and unreacted char not gasified in the gasification furnace 8 to the combustion furnace 1. The downcomer 7 connected to the collector 4 has a lower end connected through a sealer 18 to the freeboard 11 in the gasification furnace 8. A raw material supply unit 20 is arranged to supply the raw material 12 to the circulating medium 5 between the sealer 18 and the freeboard 11.

    摘要翻译： 循环流化床气化炉具有燃烧炉1，将来自燃烧炉1的燃烧废气3引入其中以收集循环介质5的旋风收集器4，用于形成流化床10的流化床气化炉8 通过下降管7引入收集在旋风收集器4中的循环介质5，并从下方供给气化剂9，并通过将原料12供给到干舷11进行气化，以及循环流路14返回 循环介质和未反应的焦炭未在气化炉8中气化到燃烧炉1中。连接到集电器4的降液管7的下端通过密封件18连接到气化炉8中的干舷11。 供给单元20被布置成将原料12供给到密封件18和干舷11之间的循环介质5。