Method and plant for the heat treatment of solids containing iron oxide using a fluidized bed reactor
    3.
    发明授权
    Method and plant for the heat treatment of solids containing iron oxide using a fluidized bed reactor 有权
    使用流化床反应器对含有氧化铁的固体进行热处理的方法和设备

    公开(公告)号:US07625422B2

    公开(公告)日:2009-12-01

    申请号:US10540435

    申请日:2003-12-01

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

    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。

    Method and plant for the heat treatment of solids containing iron oxide using a fluidized bed reactor
    4.
    发明申请
    Method and plant for the heat treatment of solids containing iron oxide using a fluidized bed reactor 有权
    使用流化床反应器对含有氧化铁的固体进行热处理的方法和设备

    公开(公告)号:US20070137435A1

    公开(公告)日:2007-06-21

    申请号:US10540435

    申请日:2003-12-01

    IPC分类号: C21B13/00

    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。

    Process and plant for reducing solids containing iron oxide
    5.
    发明申请
    Process and plant for reducing solids containing iron oxide 审中-公开
    用于还原含有氧化铁的固体的方法和装置

    公开(公告)号:US20070079666A1

    公开(公告)日:2007-04-12

    申请号:US10567821

    申请日:2004-07-16

    IPC分类号: C21B15/00

    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。

    Method and plant for the heat treatment of solids containing iron oxide
    8.
    发明授权
    Method and plant for the heat treatment of solids containing iron oxide 有权
    用于对含有氧化铁的固体进行热处理的方法和设备

    公开(公告)号:US08025836B2

    公开(公告)日:2011-09-27

    申请号:US12610821

    申请日:2009-11-02

    IPC分类号: F27B15/02

    摘要: A plant for the heat treatment of solids containing iron oxide includes a fluidized bed reactor. The reactor includes at least one gas supply tube 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 at least one gas supply tube. The gas flowing through the at least one gas supply tube entrains solids from the stationary annular fluidized bed-into the mixing chamber when passing through the upper orifice region of the at least one gas supply tube.

    摘要翻译: 用于对含有氧化铁的固体进行热处理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,并且混合室位于至少一个气体供应管的上孔区域上方。 当通过至少一个气体供应管的上孔区域时,流过至少一个气体供应管的气体将固体从固定的环形流化床引入混合室。

    Method for producing iron carbide from granulated sponge iron
    9.
    发明授权
    Method for producing iron carbide from granulated sponge iron 失效
    从造粒海绵铁生产碳化铁的方法

    公开(公告)号:US06627171B2

    公开(公告)日:2003-09-30

    申请号:US09403191

    申请日:2000-03-15

    IPC分类号: C01B3130

    摘要: Process for producing Iron carbide wherein, in a first stage, Iron ore is reduced to sponge iron using a reducing gas containing at least 90% hydrogen, on a nitrogen-free basis, to produce a sponge iron having a carbon content of less than 1% wt.; then in a second stage the sponge iron is fluidized at a temperature of 500 to 800° C. with a methane-containing fluidizing gas in a fluidized bed reactor wherein the water content of the gas in the reactor is not more than 1.5% wt., to produce a product wherein at least 85% of the iron content is in the form of Fe3C.

    摘要翻译: 生产碳化铁的方法,其中在第一阶段中,使用含氮至少90%的还原气体在无氮基础上将铁矿石还原成海绵铁,以生产碳含量小于1的海绵铁 %wt。 然后在第二阶段中,海绵铁在流化床反应器中在含有甲烷的流化气体的温度下在500至800℃的温度下流化,其中反应器中气体的含水量不超过1.5重量%。 ,以生产其中至少85%的铁含量为Fe 3 C形式的产品。

    Method and plant for producing low-temperature coke
    10.
    发明申请
    Method and plant for producing low-temperature coke 失效
    生产低温焦炭的方法和装置

    公开(公告)号:US20060278566A1

    公开(公告)日:2006-12-14

    申请号:US10540073

    申请日:2003-12-01

    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。