公开(公告)号：US20100040512A1

公开(公告)日：2010-02-18

申请号：US12603852

申请日：2009-10-22

申请人： Andreas Orth ,  Martin Hirsch ,  Peter Weber ,  Stuart Sneyd ,  Dirk Nuber ,  Michael Stroeder

发明人： Andreas Orth ,  Martin Hirsch ,  Peter Weber ,  Stuart Sneyd ,  Dirk Nuber ,  Michael Stroeder

IPC分类号： B01J8/18 ,  B01J8/24

CPC分类号： B01J8/18 ,  B01J8/1863 ,  B01J8/30 ,  B01J8/44 ,  B01J2208/00061 ,  C22B1/10 ,  C22B5/14 ,  F27B15/02 ,  F27B15/08 ,  F27B15/10

摘要： A plant for the heat treatment of solids containing iron oxide. The plant includes a reactor including a fluidized bed reactor. The reactor includes a gas supply system disposed in the reactor, a stationary annular fluidized bed which at least partly surrounds the gas supply system, and a mixing chamber. The gas supply system is configured so that gas flowing through the gas supply system entrains solids from the stationary annular fluidized bed into the mixing chamber.

摘要翻译： 用于热处理含有氧化铁的固体的设备。 该设备包括一个包括流化床反应器的反应器。 反应器包括设置在反应器中的气体供应系统，至少部分地围绕气体供应系统的固定环形流化床和混合室。 气体供应系统被配置为使得流过气体供应系统的气体将固体从固定的环形流化床引入混合室。

公开(公告)号：US07625422B2

公开(公告)日：2009-12-01

申请号：US10540435

申请日：2003-12-01

申请人： Andreas Orth ,  Martin Hirsch ,  Peter Weber ,  Stuart Sneyd ,  Dirk Nuber ,  Michael Ströder

发明人： Andreas Orth ,  Martin Hirsch ,  Peter Weber ,  Stuart Sneyd ,  Dirk Nuber ,  Michael Ströder

IPC分类号： B01J8/24 ,  C22B1/10 ,  C22B5/14

CPC分类号： B01J8/18 ,  B01J8/1863 ,  B01J8/30 ,  B01J8/44 ,  B01J2208/00061 ,  C22B1/10 ,  C22B5/14 ,  F27B15/02 ,  F27B15/08 ,  F27B15/10

摘要： The present invention relates to a method and a plant for the heat treatment of solids containing iron oxide, in which fine-grained solids are heated to a temperature of 700 to 1150° C. in a fluidized bed reactor (8). To improve the utilization of energy, it is proposed to introduce a first gas or gas mixture from below through at least one gas supply tube (9) into a mixing chamber region (15) of the reactor (8), the gas supply tube (9) being at least partly surrounded by a stationary annular fluidized bed (12) which is fluidized by supplying fluidizing gas. The gas velocities of the first gas or gas mixture and of the fluidizing gas for the annular fluidized bed (12) are adjusted such that the Particle-Froude-Numbers in the gas supply tube (9) are between 1 and 100, in the annular fluidized bed (12) between 0.02 and 2, and in the mixing chamber (15) between 0.3 and 30.

摘要翻译： 本发明涉及用于热处理包含氧化铁的固体的方法和设备，其中在流化床反应器（8）中将细粒固体加热至700至1150℃的温度。 为了提高能量的利用率，建议从下方通过至少一个气体供给管（9）将第一气体或气体混合物引入反应器（8）的混合室区域（15），气体供给管 9）至少部分地被固定的环形流化床（12）包围，所述静止环形流化床通过供应流化气体而被流化。 第一气体或气体混合物以及用于环形流化床（12）的流化气体的气体速度被调整为使得气体供应管（9）中的“微粒 - 弗劳德数”在1和100之间，在环形 流化床（12）在0.02和2之间，在混合室（15）中在0.3和30之间。

公开(公告)号：US20070137435A1

公开(公告)日：2007-06-21

申请号：US10540435

申请日：2003-12-01

申请人： Andreas Orth ,  Martin Hirsch ,  Peter Weber ,  Stuart Sneyd ,  Dirk Nuber ,  Michael Stroder

发明人： Andreas Orth ,  Martin Hirsch ,  Peter Weber ,  Stuart Sneyd ,  Dirk Nuber ,  Michael Stroder

IPC分类号： C21B13/00

CPC分类号： B01J8/18 ,  B01J8/1863 ,  B01J8/30 ,  B01J8/44 ,  B01J2208/00061 ,  C22B1/10 ,  C22B5/14 ,  F27B15/02 ,  F27B15/08 ,  F27B15/10

摘要： The present invention relates to a method and a plant for the heat treatment of solids containing iron oxide, in which fine-grained solids are heated to a temperature of 700 to 1150° C. in a fluidized bed reactor (8). To improve the utilization of energy, it is proposed to introduce a first gas or gas mixture from below through at least one gas supply tube (9) into a mixing chamber region (15) of the reactor (8), the gas supply tube (9) being at least partly surrounded by a stationary annular fluidized bed (12) which is fluidized by supplying fluidizing gas. The gas velocities of the first gas or gas mixture and of the fluidizing gas for the annular fluidized bed (12) are adjusted such that the Particle-Froude-Numbers in the gas supply tube (9) are between 1 and 100, in the annular fluidized bed (12) between 0.02 and 2, and in the mixing chamber (15) between 0.3 and 30.

摘要翻译： 本发明涉及用于热处理包含氧化铁的固体的方法和设备，其中在流化床反应器（8）中将细粒固体加热至700至1150℃的温度。 为了提高能量的利用率，建议从下方通过至少一个气体供给管（9）将第一气体或气体混合物引入反应器（8）的混合室区域（15），气体供给管 9）至少部分地被固定的环形流化床（12）包围，所述静止环形流化床通过供应流化气体而被流化。 第一气体或气体混合物以及用于环形流化床（12）的流化气体的气体速度被调整为使得气体供应管（9）中的“微粒 - 弗劳德数”在1和100之间，在环形 流化床（12）在0.02和2之间，在混合室（15）中在0.3和30之间。

公开(公告)号：US08021600B2

公开(公告)日：2011-09-20

申请号：US12603852

申请日：2009-10-22

申请人： Andreas Orth ,  Martin Hirsch ,  Peter Weber ,  Stuart Sneyd ,  Dirk Nuber ,  Michael Stroeder

发明人： Andreas Orth ,  Martin Hirsch ,  Peter Weber ,  Stuart Sneyd ,  Dirk Nuber ,  Michael Stroeder

IPC分类号： F27B15/02

CPC分类号： B01J8/18 ,  B01J8/1863 ,  B01J8/30 ,  B01J8/44 ,  B01J2208/00061 ,  C22B1/10 ,  C22B5/14 ,  F27B15/02 ,  F27B15/08 ,  F27B15/10

摘要： A plant for the heat treatment of solids containing iron oxide. The plant includes a reactor including a fluidized bed reactor. The reactor includes a gas supply system disposed in the reactor, a stationary annular fluidized bed which at least partly surrounds the gas supply system, and a mixing chamber. The gas supply system is configured so that gas flowing through the gas supply system entrains solids from the stationary annular fluidized bed into the mixing chamber.

摘要翻译： 用于热处理含有氧化铁的固体的设备。 该设备包括一个包括流化床反应器的反应器。 反应器包括设置在反应器中的气体供应系统，至少部分地围绕气体供应系统的固定环形流化床和混合室。 气体供应系统被配置为使得流过气体供应系统的气体将固体从固定的环形流化床引入混合室。

公开(公告)号：US20070079666A1

公开(公告)日：2007-04-12

申请号：US10567821

申请日：2004-07-16

申请人： Stuart Sneyd ,  Martin Hirsch ,  Dirk Nuber

发明人： Stuart Sneyd ,  Martin Hirsch ,  Dirk Nuber

IPC分类号： C21B15/00

CPC分类号： C22B5/18 ,  C21B13/0033 ,  C21B13/008 ,  C21B13/0086 ,  C22B1/248 ,  C22B5/14 ,  Y02P10/136

摘要： This invention relates to a process for reducing solids containing iron oxide, such as iron ore, in which fine-grained solids are heated and at least partly calcined in a pre-heating stage (2, 9). In a first fluidized-bed reactor (14) downstream of the preheating stage (2, 9), the solids are prereduced and reduced further in a second fluidized-bed reactor (16). Downstream of the second reactor (16) a briquetting stage (20) is provided, in which the solids are briquetted at a temperature above 500° C. To increase the energy efficiency of the process and improve the flowability of the solids in the briquetting stage (20), magnesite is added to the preheating stage (2, 9) together with the solids containing iron oxide, which magnesite is at least partly calcined in the preheating stage (2, 9) to obtain magnesium oxide. Furthermore, the invention relates to a corresponding plant.

摘要翻译： 本发明涉及一种用于还原含铁氧化物的固体的方法，例如铁矿石，其中细粒固体被加热并且在预热阶段（2,9）中至少部分地煅烧。 在预热阶段（2,9）下游的第一流化床反应器（14）中，固体在第二流化床反应器（16）中被进一步还原并还原。 在第二反应器（16）的下游提供压块级（20），其中固体在500℃以上的压块压块。为了提高该方法的能量效率并提高压块阶段的固体的流动性 （20）中，将菱镁矿与含有氧化铁的固体一起加入到预热段（2,9）中，该氧化铁在预热阶段（2,9）中至少部分地煅烧以获得氧化镁。 此外，本发明涉及相应的设备。

公开(公告)号：US20100074805A1

公开(公告)日：2010-03-25

申请号：US12628479

申请日：2009-12-01

申请人： Dirk Nuber ,  Michael Stroeder ,  Werner Stockhausen ,  Ali-Naghi Beyzavi ,  Lothar Formanek ,  Martin Hirsch

发明人： Dirk Nuber ,  Michael Stroeder ,  Werner Stockhausen ,  Ali-Naghi Beyzavi ,  Lothar Formanek ,  Martin Hirsch

IPC分类号： B01J8/24

CPC分类号： B01J8/1818 ,  B01J8/1836 ,  B01J8/26 ,  B01J2208/00548 ,  B01J2208/00725 ,  C21B13/0033 ,  C22B1/10 ,  C22B5/14 ,  C22B34/1204 ,  C22B34/1209 ,  F27B15/02 ,  F27B15/10 ,  Y02P10/136

摘要： A plant for the heat treatment of solids containing titanium includes a fluidized bed reactor. The reactor includes at least one gas supply tube being at least partly surrounded by an annular chamber in which a stationary annular fluidized bed is located, and a mixing chamber being located above the upper orifice region of the gas supply tube. The gas flowing through the gas supply tube entrains solids from the stationary annular fluidized bed into the mixing chamber when passing through the upper orifice region of the gas supply system. The plant further includes a solids separator downstream of the reactor. The solids separator includes a solids conduit leading to the annular fluidized bed of the reactor.

摘要翻译： 用于热处理含钛固体的设备包括流化床反应器。 反应器包括至少一个气体供应管，其至少部分地被环形室围绕，其中定位有固定环形流化床，并且混合室位于气体供应管的上孔区域上方。 流过气体供应管的气体在通过气体供应系统的上部孔口区域时将固体从固定的环形流化床引入混合室。 该设备还包括在反应器下游的固体分离器。 固体分离器包括通向反应器的环形流化床的固体导管。

公开(公告)号：US08021601B2

公开(公告)日：2011-09-20

申请号：US12628479

申请日：2009-12-01

申请人： Dirk Nuber ,  Michael Stroeder ,  Werner Stockhausen ,  Lothar Formanek ,  Martin Hirsch ,  Ali-Naghi Beyzavi

发明人： Dirk Nuber ,  Michael Stroeder ,  Werner Stockhausen ,  Lothar Formanek ,  Martin Hirsch ,  Ali-Naghi Beyzavi

IPC分类号： F27B15/02

CPC分类号： B01J8/1818 ,  B01J8/1836 ,  B01J8/26 ,  B01J2208/00548 ,  B01J2208/00725 ,  C21B13/0033 ,  C22B1/10 ,  C22B5/14 ,  C22B34/1204 ,  C22B34/1209 ,  F27B15/02 ,  F27B15/10 ,  Y02P10/136

摘要： A plant for the heat treatment of solids containing titanium includes a fluidized bed reactor. The reactor includes at least one gas supply tube being at least partly surrounded by an annular chamber in which a stationary annular fluidized bed is located, and a mixing chamber being located above the upper orifice region of the gas supply tube. The gas flowing through the gas supply tube entrains solids from the stationary annular fluidized bed into the mixing chamber when passing through the upper orifice region of the gas supply system. The plant further includes a solids separator downstream of the reactor. The solids separator includes a solids conduit leading to the annular fluidized bed of the reactor.

摘要翻译： 用于热处理含钛固体的设备包括流化床反应器。 反应器包括至少一个气体供应管，其至少部分地被环形室围绕，其中定位有固定环形流化床，并且混合室位于气体供应管的上孔区域上方。 流过气体供应管的气体在通过气体供应系统的上部孔口区域时将固体从固定的环形流化床引入混合室。 该设备还包括在反应器下游的固体分离器。 固体分离器包括通向反应器的环形流化床的固体导管。

公开(公告)号：US07651547B2

公开(公告)日：2010-01-26

申请号：US10540376

申请日：2003-12-10

申请人： Dirk Nuber ,  Michael Ströder ,  Werner Stockhausen ,  Ali-Naghi Beyzavi ,  Lothar Formanek ,  Martin Hirsch

发明人： Dirk Nuber ,  Michael Ströder ,  Werner Stockhausen ,  Ali-Naghi Beyzavi ,  Lothar Formanek ,  Martin Hirsch

IPC分类号： B01J8/24 ,  C22B1/10 ,  C22B5/14

CPC分类号： B01J8/1818 ,  B01J8/1836 ,  B01J8/26 ,  B01J2208/00548 ,  B01J2208/00725 ,  C21B13/0033 ,  C22B1/10 ,  C22B5/14 ,  C22B34/1204 ,  C22B34/1209 ,  F27B15/02 ,  F27B15/10 ,  Y02P10/136

摘要： The present invention relates to a method and a plant for the heat treatment of solids containing titanium and possibly further metal oxides, in which fine-grained solids are heated to a temperature of 700 to 950° C. in a fluidized bed reactor (1). To improve the energy utilization, it is proposed to introduce a first gas or gas mixture from below through a gas supply tube (3) into a mixing chamber (7) of the reactor (1), the gas supply tube (3) being at least partly surrounded by a stationary annular fluidized bed (10) which is fluidized by supplying fluidizing gas. The gas velocities of the first gas or gas mixture as well as of the fluidizing gas for the annular fluidized bed (10) are adjusted such that the particle Froude numbers in the gas supply tube (3) are between 1 and 100, in the annular fluidized bed (10) between 0.02 and 2 and in the mixing chamber (7) between 0.3 and 30.

摘要翻译： 本发明涉及用于热处理包含钛和可能的其它金属氧化物的固体的方法和设备，其中在流化床反应器（1）中将细粒固体加热至700-950℃， 。 为了提高能量利用率，建议从下方通过气体供给管（3）将第一气体或气体混合物引入反应器（1）的混合室（7），气体供给管（3）处于 最少部分地被固定的环形流化床（10）包围，所述静止环形流化床通过供应流化气体而流化。 调节第一气体或气体混合物以及用于环形流化床（10）的流化气体的气体速度，使得气体供应管（3）中的微粒弗劳德数在1和100之间，在环形 流化床（10）在0.02和2之间，并且在混合室（7）中在0.3和30之间。

公开(公告)号：US20060162500A1

公开(公告)日：2006-07-27

申请号：US10540376

申请日：2003-12-10

申请人： Dirk Nuber ,  Michael Stroder ,  Werner Stockhausen ,  Ali-Naghi Beyzavi ,  Lothar Formanek ,  Martin Hirsch

发明人： Dirk Nuber ,  Michael Stroder ,  Werner Stockhausen ,  Ali-Naghi Beyzavi ,  Lothar Formanek ,  Martin Hirsch

IPC分类号： C22B34/12

CPC分类号： B01J8/1818 ,  B01J8/1836 ,  B01J8/26 ,  B01J2208/00548 ,  B01J2208/00725 ,  C21B13/0033 ,  C22B1/10 ,  C22B5/14 ,  C22B34/1204 ,  C22B34/1209 ,  F27B15/02 ,  F27B15/10 ,  Y02P10/136

摘要： The present invention relates to a method and a plant for the heat treatment of solids containing titanium and possibly further metal oxides, in which fine-grained solids are heated to a temperature of 700 to 950° C. in a fluidized bed reactor (1). To improve the energy utilization, it is proposed to introduce a first gas or gas mixture from below through a gas supply tube (3) into a mixing chamber (7) of the reactor (1), the gas supply tube (3) being at least partly surrounded by a stationary annular fluidized bed (10) which is fluidized by supplying fluidizing gas. The gas velocities of the first gas or gas mixture as well as of the fluidizing gas for the annular fluidized bed (10) are adjusted such that the particle Froude numbers in the gas supply tube (3) are between 1 and 100, in the annular fluidized bed (10) between 0.02 and 2 and in the mixing chamber (7) between 0.3 and 30.

摘要翻译： 本发明涉及用于热处理包含钛和可能的其它金属氧化物的固体的方法和设备，其中在流化床反应器（1）中将细粒固体加热至700-950℃， 。 为了提高能量利用率，建议从下方通过气体供给管（3）将第一气体或气体混合物引入反应器（1）的混合室（7），气体供给管（3）处于 最少部分地被固定的环形流化床（10）包围，所述静止环形流化床通过供应流化气体而被流化。 调节第一气体或气体混合物以及用于环形流化床（10）的流化气体的气体速度，使得气体供应管（3）中的微粒弗劳德数在1和100之间，在环形 流化床（10）在0.02和2之间，并且在混合室（7）中在0.3和30之间。

公开(公告)号：US07854608B2

公开(公告)日：2010-12-21

申请号：US10540436

申请日：2003-12-10

申请人： Dirk Nuber ,  Werner Stockhausen ,  Michael Ströder

发明人： Dirk Nuber ,  Werner Stockhausen ,  Michael Ströder

IPC分类号： B01J8/24 ,  C22B1/10 ,  C22B5/14

CPC分类号： B01J8/1836 ,  B01J8/0055 ,  B01J8/1863 ,  B01J2208/00141 ,  B01J2208/0053 ,  B01J2208/00548 ,  B01J2208/00654 ,  B01J2219/00006 ,  C04B11/0283 ,  F27B15/02 ,  F27B15/10 ,  F27B15/16

摘要： The present invention relates to a method for the heat treatment of fine-grained solids, in particular gypsum, in which the solids are heated to a temperature of 50 to 1000° C. in a fluidized bed reactor (1), and to a corresponding plant. To improve the energy utilization, it is proposed to introduce a first gas or gas mixture from below through a preferably central gas supply tube (3) into a mixing chamber (21) of the reactor (1), the gas supply tube (3) being at least partly surrounded by a stationary annular fluidized bed (2) which is fluidized by supplying fluidizing gas, and to adjust the gas velocities of the first gas or gas mixture as well as of the fluidizing gas for the annular fluidized bed (2) such that the particle Froude numbers in the gas supply tube (3) are between 1 and 100, in the annular fluidized bed (2) between 0.02 and 2 and in the mixing chamber (21) between 0.3 and 30.

摘要翻译： 本发明涉及一种用于热处理细粒固体，特别是石膏的方法，其中将固体在流化床反应器（1）中加热至50至1000℃的温度，以及相应的 厂。 为了提高能量利用率，建议从下方通过优选的中心气体供给管（3）将第一气体或气体混合物引入反应器（1）的混合室（21），气体供给管（3） 至少部分地被固定的环形流化床（2）包围，所述静止环形流化床（2）通过供应流化气体而流化，并且调节第一气体或气体混合物以及用于环形流化床（2）的流化气体的气体速度， 使得气体供给管（3）中的微粒Froude数在1和100之间，在0.02和2之间的环形流化床（2）和在0.3和30之间的混合室（21）中。