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    • 1. 再颁专利
    • Method and plant utilizing fine coal in a melter gasifier
    • 在熔化炉气化炉中利用细煤的方法和设备
    • USRE39536E1
    • 2007-04-03
    • US10160864
    • 2002-05-30
    • Günter SchreyParviz Zahedi
    • Günter SchreyParviz Zahedi
    • C21B11/00
    • C21B13/002
    • In a method for the production of liquid metal, in particular liquid pig iron (9) or liquid steel pre-products, from metal carriers, in particular partially reduced or reduced sponge iron (3), in a melter gasifier (1) in which with supply of a carbon-containing material at least partially formed of fine coal (16) and coal dust (13) and with supply of oxygen or oxygen-containing gas the metal carriers are melted in a bed (4) of the carbon-containing material at the simultaneous formation of a reducing gas, optionally upon previous final reduction, fine coal (16) and coal dust (13) which are being charged, are mixed with bitumen (20) in the hot state, after undergoing a drying operation, and subsequently are cold-briquetted, and the briquettes (25) thus formed are charged to the melter gasifier (1) in the cold state and in the melter gasifier (1) are subjected to shock-heating.
    • 在一种熔融气化炉(1)中从金属载体,特别是部分还原或还原的海绵铁(3)生产液态金属,特别是液态生铁(9)或液态钢前产品的方法中,其中 供应至少部分由细煤(16)和煤尘(13)形成的含碳材料,并且供应氧气或含氧气体,金属载体在含碳的床(4)中熔化 在进行干燥操作时,在同时形成还原气体的材料中,任选地在先前的最终还原之后,正在充电的细煤(16)和煤尘(13)在热状态下与沥青(20)混合, 然后将其压冷,将这样形成的块状物(25)在冷态下装入熔化器气化器(1),并在熔融气化器(1)中进行冲击加热。
    • 2. 发明授权
    • Method and plant of utilizing fine coal in a melter gasifier
    • 在熔化炉气化炉中利用细煤的方法和装置
    • US06332911B1
    • 2001-12-25
    • US09476239
    • 1999-12-30
    • Günter SchreyParviz Zahedi
    • Günter SchreyParviz Zahedi
    • C21B1100
    • C21B13/0006C10L5/16C10L5/361C21B13/002C21B13/0066C21B13/14
    • In a method for the production of liquid metal, in particular liquid pig iron (9) or liquid steel pre-products, from metal carriers, in particular partially reduced or reduced sponge iron (3), in a melter gasifier (1) in which with supply of a carbon-containing material at least partially formed of fine coal (16) and coal dust (13) and with supply of oxygen or oxygen-containing gas the metal carriers are melted in a bed (4) of the carbon-containing material at the simultaneous formation of a reducing gas, optionally upon previous final reduction, fine coal (16) and coal dust (13) which are being charged, are mixed with bitumen (20) in the hot state, after undergoing a drying operation, and subsequently are cold-briquetted, and the briquettes (25) thus formed are charged to the melter gasifier (1) in the cold state and in the melter gasifier (1) are subjected to shock-heating.
    • 在一种熔融气化炉(1)中从金属载体,特别是部分还原或还原的海绵铁(3)生产液态金属,特别是液态生铁(9)或液态钢前产品的方法中,其中 供应至少部分由细煤(16)和煤尘(13)形成的含碳材料,并且供应氧气或含氧气体,金属载体在含碳的床(4)中熔化 在进行干燥操作时,在同时形成还原气体的材料中,任选地在先前的最终还原之后,正在充电的细煤(16)和煤尘(13)在热状态下与沥青(20)混合, 然后将其压冷,将这样形成的块状物(25)在冷态下装入熔化器气化器(1),并在熔融气化器(1)中进行冲击加热。
    • 3. 发明授权
    • Method of reducing the number of pollutants in a gas flow and device for carrying out said method
    • 降低气流中污染物数量的方法及其实施方法
    • US06511529B1
    • 2003-01-28
    • US09180805
    • 2002-06-07
    • Karin PichlerGünter SchreyAlfred Hirsch
    • Karin PichlerGünter SchreyAlfred Hirsch
    • B01D4706
    • B01D47/00C02F2103/18C10K1/101
    • The object of the invention is to provide a method of treating wash water resulting from the scrubbing of process gases in smelting plants, according to which method the wash water is brought into intimate contact with the process gas and is circulated when the solids have been deposited. The method according to the invention draws off a partial flow from the wash water, mixes it with fresh water and uses it for rewashing the process gas. According to the invention, the wash water necessary for the scrubbers is drawn from a wash water container. In the sedimentation tank the insoluble portions are removed from the substance-charged wash water which is then introduced into the wash water container. The wash water required for the rewashing stage is removed from the wash water container and mixed with fresh water via the fresh water pipe. Solids are likewise removed in the sedimentation tank from the wash water from the rewashing stage, this wash water then being, circulated after introduction into the wash water container.
    • 本发明的目的是提供一种处理由冶炼厂中的工艺气体洗涤产生的洗涤水的方法,根据该方法,洗涤水与工艺气体紧密接触并在固体沉积时循环 。 根据本发明的方法从洗涤水中排出部分流动,将其与淡水混合并将其用于对工艺气体进行再洗涤。 根据本发明,洗涤器所需的洗涤水从洗涤水容器中抽出。 在沉淀池中,将不溶部分从装有物质的洗涤水中除去,然后将其引入洗涤水容器中。 冲洗阶段所需的洗涤水从洗涤水容器中取出,并通过淡水管与淡水混合。 固体同样从沉淀池中从洗涤阶段的洗涤水中除去,然后洗涤水在引入洗涤水容器之后循环。
    • 4. 发明授权
    • Process for the production of liquid pig iron or liquid intermediate products of steel
    • 生产液态生铁或钢液中间体的工艺
    • US06251162B1
    • 2001-06-26
    • US09125869
    • 1998-10-26
    • Ernst EichbergerGünter SchreyFranz ReuferJörg DiehlGerald Rosenfellner
    • Ernst EichbergerGünter SchreyFranz ReuferJörg DiehlGerald Rosenfellner
    • C21B1100
    • C21B13/002C21B13/14C21B2100/282C21B2100/42C21B2100/44C21B2100/66Y02P10/122Y02P10/126Y02P10/128Y02P10/136
    • In a method for producing liquid pig iron or liquid steel pre-products from charging substances comprising iron ore, preferably in lumps or pellets, and optionally fluxes. The charging substances are directly reduced to sponge iron in a reduction zone (12) and the sponge iron is melted in a melt-down gasifying zone (8) under the supply of carbon carriers and oxygen-containing gas. CO-and H2-containing gas is introduced into the reduction zone (12) and is reacted there. An export gas is withdrawn and conducted to a consumer (20). The export gas is subjected to CO2 removal or partial combustion and the resulting gas with CO2 is introduced back into the reduction process. This is done to keep down the carbon carriers having high portion of Cfix as well as consumption of O2. A highly CO2-containing gas having a CO2 content far in excess of the CO2 content of the export gas, preferably exceeding 40%, and having a CO content that is far below the CO content of the export gas is introduced into the melt-down gasifying zone (8).
    • 在由含铁矿石,优选为块状或丸状物以及任选的助熔剂的填充物质生产液体生铁或液态钢预产品的方法中。 充电物质在还原区(12)中直接还原成海绵铁,并且在碳载体和含氧气体的供应下,在熔融气化区(8)中将海绵铁熔化。 将含CO和H 2的气体引入还原区(12)中并在其中反应。 出口气体被撤回并传送给消费者(20)。 出口气体经过二氧化碳去除或部分燃烧,所产生的带有二氧化碳的气体被引回还原过程。 这样做是为了阻止具有高Cfix部分的碳载体以及O2的消耗。 将CO 2含量远远超过出口气体的CO 2含量,优选超过40%,并且具有远低于出口气体的CO含量的CO含量的高含CO 2气体被引入熔体 气化区(8)。