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：US07803268B2

公开(公告)日：2010-09-28

申请号：US10540073

申请日：2003-12-01

申请人： Andreas Orth ,  Martin Hirsch ,  Peter Weber

发明人： Andreas Orth ,  Martin Hirsch ,  Peter Weber

IPC分类号： C10G9/14 ,  B01J8/18

CPC分类号： C10B49/10 ,  C10B53/04

摘要： The present invention relates to a method and a plant for producing low 15 temperature coke, in which granular coal and possibly further solids are heated to a temperature of 700 to 1050° C. in a fluidized-bed reactor (2) by means of an oxygen-containing gas. 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 (3) into a mixing chamber region (8) of the reactor (2), the gas supply tube (3) being at least partly surrounded by a stationary annular fluidized bed (6) 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 (6) are adjusted such that the Particle-Froude-Numbers in the gas supply tube (3) are between 1 and 100, in the annular fluidized bed (6) between 0.02 and 2 and in the 25 mixing chamber (8) between 0.3 and 30.

摘要翻译： 本发明涉及一种用于生产低温度焦炭的方法和设备，其中颗粒煤和可能的其它固体在流化床反应器（2）中通过以下方式加热至700至1050℃的温度： 含氧气体。 为了提高能量利用率，建议从下方将至少一个气体供给管（3）的第一气体或气体混合物引入反应器（2）的混合室区域（8），气体供给管（3） ）至少部分地被固定的环形流化床（6）包围，所述固定环形流化床通过供应流化气体而被流化。 调整第一气体或气体混合物和用于环形流化床（6）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”为1至100，在环形 流化床（6）在0.02和2之间，在25混合室（8）中在0.3和30之间。

公开(公告)号：US06688474B1

公开(公告)日：2004-02-10

申请号：US09700358

申请日：2000-11-13

申请人： Martin Hirsch ,  Andreas Orth ,  Peter Weber

发明人： Martin Hirsch ,  Andreas Orth ,  Peter Weber

IPC分类号： B07B400

CPC分类号： F27B15/02 ,  B01J8/0025 ,  B01J8/1872

摘要： According to the invention, a fluidizing gas is introduced upwards into the fluidized bed (3) through a valve grid (2), said stationary fluidized bed (3) containing solids with different grain sizes. A supply pipe (10) is disposed in the area of the fluidized bed, the mouth of said pipe being located above the valve grid (2) and its outlet (12) leading outwards from the fluidized bed (3). Part of the solids located above the valve grid (2) is blown into the supply pipe by a gas jet (13) which is directed upwards and fed separately from the fluidizing gas and pneumatically evacuated from the fluidized bed through the supply pipe (10). Normally, the flow speed of the gas in the supply pipe is at least two times higher than the speed of the fluidizing gas in the fluidized bed.

摘要翻译： 根据本发明，流化气体通过阀网格（2）向上引入流化床（3），所述固定流化床（3）含有不同晶粒尺寸的固体。 供给管（10）设置在流化床的区域中，所述管的口位于阀网格（2）的上方，以及从流化床（3）向外导出的出口（12）。 位于阀网格（2）上方的固体的一部分通过气体射流（13）吹送到供应管中，该气体射流（13）被引导向上并与流化气体分开供给，并通过供应管道（10）从流化床气动抽真空， 。 通常，供给管中的气体的流速比流化床中的流化气体的速度高至少两倍。

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：US20060278566A1

公开(公告)日：2006-12-14

申请号：US10540073

申请日：2003-12-01

申请人： Andreas Orth ,  Martin Hirsch ,  Peter Weber

发明人： Andreas Orth ,  Martin Hirsch ,  Peter Weber

IPC分类号： C10G9/14 ,  B01J8/18

CPC分类号： C10B49/10 ,  C10B53/04

摘要： The present invention relates to a method and a plant for producing low 15 temperature coke, in which granular coal and possibly further solids are heated to a temperature of 700 to 1050° C. in a fluidized-bed reactor (2) by means of an oxygen-containing gas. 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 (3) into a mixing chamber region (8) of the reactor (2), the gas supply tube (3) being at least partly surrounded by a stationary annular fluidized bed (6) 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 (6) are adjusted such that the Particle-Froude-Numbers in the gas supply tube (3) are between 1 and 100, in the annular fluidized bed (6) between 0.02 and 2 and in the 25 mixing chamber (8) between 0.3 and 30.

摘要翻译： 本发明涉及一种用于生产低温度焦炭的方法和设备，其中颗粒煤和可能的其它固体在流化床反应器（2）中通过以下方式加热至700至1050℃的温度： 含氧气体。 为了提高能量利用率，建议从下方将至少一个气体供给管（3）的第一气体或气体混合物引入反应器（2）的混合室区域（8），气体供给管（3） ）至少部分地被固定的环形流化床（6）包围，所述固定环形流化床通过供应流化气体而被流化。 调整第一气体或气体混合物和用于环形流化床（6）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”为1至100，在环形 流化床（6）在0.02和2之间，在25混合室（8）中在0.3和30之间。

公开(公告)号：US5667556A

公开(公告)日：1997-09-16

申请号：US643463

申请日：1996-05-03

申请人： Andreas Orth ,  Peter Weber ,  Uwe Harter ,  Ernst Wallis

发明人： Andreas Orth ,  Peter Weber ,  Uwe Harter ,  Ernst Wallis

IPC分类号： C22B5/14 ,  C22B7/02 ,  C22B19/04 ,  C22B19/28 ,  C22B19/30 ,  C22B7/00

CPC分类号： C22B7/02 ,  C22B19/04 ,  C22B19/28 ,  C22B5/14 ,  Y02P10/212 ,  Y10S75/961

摘要： This invention describes a method of reprocessing zinc- and iron oxide-containing residual material. Zinc- and iron oxide-containing dust and/or sludge is granulated with water, granules and carbonaceous material are fed to a circulating fluidized bed system, the gas-solids suspension circulated in the circulating fluidized bed system is fed to a second fluidized bed reactor, the solids discharged from the second fluidized bed reactor are recycled to the reactor of the circulating fluidized bed system, 50 to 75% by volume of the oxygen required to gasify the carbonaceous material are fed as fluidizing gas to the reactor of the circulating fluidized bed system and 25 to 50% by volume of said required oxygen are fed as a fluidizing gas and secondary gas to the second fluidized bed reactor, iron oxide-containing material is discharged from the reactor of the circulating fluidized bed system and zinc-containing material is discharged with the exhaust gas from the circulating fluidized bed system.

摘要翻译： 本发明描述了一种重新处理含锌和氧化铁的残留材料的方法。 含锌和氧化铁的粉尘和/或污泥用水造粒，颗粒和碳质材料进料到循环流化床系统中，在循环流化床系统中循环的气固体悬浮液进料到第二流化床反应器 将从第二流化床反应器排出的固体再循环到循环流化床系统的反应器中，气化碳质物质所需的50至75体积％的氧气作为流化气体供入循环流化床的反应器 系统和25〜50体积％的所需氧气作为流化气体和二次气体供给到第二流化床反应器，含氧化铁的材料从循环流化床系统的反应器排出，含锌材料为 从循环流化床系统排出废气。

公开(公告)号：US20060230880A1

公开(公告)日：2006-10-19

申请号：US10540434

申请日：2003-12-12

申请人： Martin Hirsch ,  Michael Ströder ,  Peter Weber

发明人： Martin Hirsch ,  Michael Ströder ,  Peter Weber

IPC分类号： C21B13/00

CPC分类号： B01J8/0055 ,  B01J8/1827 ,  B01J8/1872 ,  B01J2208/00274 ,  B01J2208/00548 ,  B01J2219/00006 ,  C21B13/0033 ,  C22B5/14 ,  Y02P10/136

摘要： A method for the heat treatment of solids containing iron oxide, in which fine-grained solids are heated to a temperature of about 630° C. in a fluidized-bed reactor (1). To improve the utilization of energy, it is proposed to introduce a first gas or gas mixture from below through a 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 and of the fluidizing gas for the annular fluidized bet (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： 一种用于热处理含有氧化铁的固体的方法，其中在流化床反应器（1）中将细粒固体加热至约630℃的温度。 为了提高能量的利用率，提出从下方将第一气体或气体混合物从供给管（3）引入到反应器（1）的混合室（7）中，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。 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被调节，使得气体供应管（3）中的粒子 - 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：US6074456A

公开(公告)日：2000-06-13

申请号：US77780

申请日：1998-12-21

申请人： Jochen Freytag ,  Helmut Hausmann ,  Martin Hirsch ,  Siegfried Schimo ,  Michael Stroder ,  Peter Weber

发明人： Jochen Freytag ,  Helmut Hausmann ,  Martin Hirsch ,  Siegfried Schimo ,  Michael Stroder ,  Peter Weber

IPC分类号： C21B13/00 ,  C22B1/24 ,  B02C17/00

CPC分类号： C21B13/0086 ,  C22B1/24

摘要： The granular sponge iron is supplied to a roller press at temperatures of 600 to 850.degree. C. for molding the hot briquets. There is produced a strip structure of sponge iron containing formed hot briquets, which are arranged at a distance from each other. By smashing the strip structure, the hot briquets are separated from each other, so that fragments of the strip structure are obtained. The hot briquets and at least part of the fragments are cooled to temperatures in the range from 20 to 400.degree. C., and the cooled briquets and fragments are passed through a rotary drum. In the rotary drum, fine-grained fines of the briquets and fragments are produced. Subsequently, these fines are separated from the briquets and fragments, as they exhibit a pyrophoric behavior.

摘要翻译： PCT No.PCT / EP96 / 05446 Sec。 371 1998年12月21日第 102（e）日期1998年12月21日PCT提交1996年12月5日PCT公布。 出版物WO97 / 21840 日期1996年6月19日将粒状海绵铁在600〜850℃的温度下供给到辊压机中，以成型热土坯。 产生含有形成的热砖的海绵铁带状结构，它们彼此间隔一定距离。 通过粉碎带状结构，将热块彼此分离，从而获得带状结构的碎片。 将热块和至少部分碎片冷却至20至400℃的温度，并将冷却的块状物和碎片通过旋转鼓。 在旋转鼓中，生产细粒和碎片的细粒。 随后，这些罚款与砖块和碎片分离，因为它们具有自燃行为。