METHOD AND DEVICE FOR TREATING PARTICULATE MATERIAL
    1.
    发明申请
    METHOD AND DEVICE FOR TREATING PARTICULATE MATERIAL 审中-公开
    方法和装置处理粒料

    公开(公告)号:WO02103063A2

    公开(公告)日:2002-12-27

    申请号:PCT/EP0205856

    申请日:2002-05-28

    CPC classification number: B04C5/22 B04C5/00 C21B13/0033 F27B15/00 Y02P10/136

    Abstract: The invention relates to a method for treating, preferably for reducing, particulate material in at least one fluidization zone at an increased temperature, particularly for reducing ore dust. According to the method, the particulate material is held in the fluidization zone by a treatment gas that flows upward from the bottom, and fine-particulate material, which is transported out of the fluidization zone with the treatment gas is separated from the treatment gas in a separating zone. To this end, the following steps are carried out in the separating zone: feeding the stream, which consists of treatment gas and of transported fine-particulate material, to a separating device (8); separating the fine-particulate material from the treatment gas, whereby the treatment gas is extracted from the separating device as waste gas, and; withdrawing the separated fine-particulate material out of the separating device (8). The invention also relates to a device for carrying out the method. Coarse grained material is introduced into the separating zone whereby reducing the amount of baked on material and deposits thereof.

    Abstract translation: 本发明涉及用于治疗,优选地用于减少,颗粒材料在至少一个流化区在升高的温度,特别是用于减少细矿的方法,其中所述颗粒材料从与所述处理气体保持通过从底部到顶部的处理气体在流化区,并且其中流动的 所述流化材料排出细颗粒材料被沉积在从处理气体的沉积区,从而在分离区中进行以下步骤:将处理气体流和ausgetragenem细颗粒材料到分离器(8),从处理气体中分离微细颗粒材料,所述 处理气体抽出,作为流出物从所述分离装置,并排出从所述分离装置(8),以及用于执行该方法的装置所分离的细颗粒物质。 在分离区中粗粒材料被引入,由此结块和沉积物减少。

    METHOD AND DEVICE FOR PRODUCING PIG IRON AND/OR PIG IRON INTERMEDIATE PRODUCTS
    2.
    发明申请
    METHOD AND DEVICE FOR PRODUCING PIG IRON AND/OR PIG IRON INTERMEDIATE PRODUCTS 审中-公开
    方法和设备生产的金属和/或金属前兆

    公开(公告)号:WO03068994A8

    公开(公告)日:2003-12-24

    申请号:PCT/EP0301280

    申请日:2003-02-10

    Inventor: NAGL MICHAEL

    CPC classification number: C21B13/002 C21B13/0033 C21B13/14 C21B2100/44

    Abstract: The invention relates to a device and method for producing pig iron and/or pig iron intermediate products, according to which a metal-containing feed material is melted inside a melting unit (1) during which a working gas that, in particular, at least partially reduces is produced inside the melting unit (1), whereupon the produced working gas is evacuated. The evacuated working gas, optionally after undergoing a purification, is used, in particular, as a delivery gas for effecting, at least in part, a preferably pneumatic transport of an, in particular, fine particulate, at least partially reduced metal-containing material.

    Abstract translation: 本发明涉及的装置和用于制造金属和/或初级金属产品的方法,特别是生铁和/或生铁的前体,其特征在于,含金属供给材料在熔化单元(1)熔化,并在熔化单元(1)另外一个特别是至少部分地减少工作气体 生产和产生的工作气体被抽出。 在此,工作气体排出,任选地纯化后,特别是作为载气,至少部分于特定细颗粒的优选气动输送,至少部分还原的含金属的材料。

    4.
    发明专利
    未知

    公开(公告)号:BR0210455A

    公开(公告)日:2004-08-17

    申请号:BR0210455

    申请日:2002-05-28

    Abstract: A process and apparatus for reducing material in particle form in a fluidization zone and at elevated temperature, in particular for reducing fine ore, the particle material being held in the fluidization zone by a treatment gas which flows upward from below. Material in fine particle form is discharged from the fluidization zone with the treatment gas and is separated out of the treatment gas in a deposition zone. In the deposition zone, the stream of treatment gas and discharged material in fine particle form are fed into a separating device which removes the fine particle material from the treatment gas, the treatment gas is extracted from the separating device as off-gas, and the separated fine particle material is removed from the separating device. Coarse-grained material is then introduced into the deposition zone. This reduces the levels of caking and deposits of the fine particle material. A device for carrying out the process includes elements defining the zones.

    6.
    发明专利
    未知

    公开(公告)号:DE59606821D1

    公开(公告)日:2001-05-31

    申请号:DE59606821

    申请日:1996-07-18

    Inventor: NAGL MICHAEL

    Abstract: PCT No. PCT/AT96/00128 Sec. 371 Date Apr. 18, 1997 Sec. 102(e) Date Apr. 18, 1997 PCT Filed Jul. 18, 1996 PCT Pub. No. WO97/04136 PCT Pub. Date Feb. 6, 1997In a process for the production of molten pig iron (12) or steel pre-products from fine particulate iron-containing material, in particular reduced sponge iron, in a meltdown gasifying zone (6) of a melter gasifier (5) the iron-containing material is melted in a bed (16) formed of solid carbon carriers, under the supply of carbon-containing material and oxygen-containing gas at the simultaneous formation of a reducing gas. To prevent the fine particles of the iron-containing material charged to the melter gasifier from being discharged, the iron-containing material is supplied into the a melter gasifier (5) centrally, closely above the bed (16) but in its immediate vicinity, by means of an oxygen-burner (15) under the formation of a high-temperature combustion zone (21).

    Method for producing liquid pig iron or steel fabricated materials and installation for implementing said method

    公开(公告)号:AU4444497A

    公开(公告)日:1998-05-05

    申请号:AU4444497

    申请日:1997-10-06

    Abstract: According to a process for producing pig iron (10) from fine-particulate iron oxide carriers and lumpy iron-containing material in a meltdown gasifying zone (9) of a melter gasifier (3), the iron-containing material is melted in a bed (13) formed of solid carbon carriers, under the supply of carbon-containing material and oxygen-containing gas while simultaneously forming a reducing gas. Fine-particulate iron-oxide carriers, such as iron-containing fine ore and ore dust and oxidic iron fine dust, are introduced into a reducing gas stream leaving the melter gasifier (3), and the reducing gas is separated from the fine-particulate material formed thereby. The separated fine-particulate material is introduced into the meltdown gasifying zone (9) via a dust recirculation line (26, 27, 28, 29) and through a dust burner (30), and the reducing gas is used for reducing iron-oxide-containing material. To be able to charge large amounts of fine ore or ore dust in this process, the separated fine-particulate material in the dust recirculation line (26 to 29) is conveyed via a fluidized bed sluice (25) formed by the separated fine-particulate material and by reducing gas to the dust burner (30) and reduced thereby (FIG. 1).

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