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Economical Iron Production in the Submerged Arc Furnace

机译:埋弧炉的经济铁生产

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In examining the historical past for iron making using a submerged arc furnace (SAF), a primary reason that this method of iron making has not dominated the industry was the cost of electricity. Submerged arc furnace production of pig iron and foundry iron has been practiced in some industrialized countries as late as the 1950's. This was especially true where coking coals were scarce, and hydroelectric power was abundant and cheap. These electric furnace iron processes used combinations of ores and fluxes to produce iron with compositions and metal to slag ratios similar to those produced in a blast furnace. Nevertheless, the quantity of electricity consumed to produce the iron was on the order of 2,300 kilowatt hours per net ton (kWH/NT). With the strong growth in the demand for electricity for other uses, and the availability of cheap iron from blast furnaces, it became apparent that only producers in countries having readily available ores and abundant hydroelectric power, such as Norway or Venezuela, were capable of economical electric iron making. Although research to improve SAF performance continued vigorously with new process developments, such as Tysland-Hole, Strategic-Udy, and New Zealand Steel, the improvements were focused on pre-reduction and pre-heating of the iron oxides prior to charging. Electricity used for those ore-based processes remained above 900 kWH/NT. With a few exceptions, none of those processes were able to demonstrate viable economics for competing with the blast furnace for steel making or the cupola for iron castings. This paper will introduce the Alabama Power Company (APC) process for making foundry iron and hot metal. This process is scrap-based and has produced foundry iron with an average of 3.4% carbon, 2.0% silicon, and 0.06% sulfur (by weight). Average energy consumption was 474 kWH/NT for foundry iron. Hot metal (4.7% C, 0.6% Si, and 0.002% S) was produced from DRI at an energy consumption of 580 kWH/NT.
机译:在研究使用埋弧炉(SAF)进行炼铁的历史时,这种炼铁方法并未在整个工业中占主导地位的主要原因是电费。到1950年代末,在一些工业化国家已经开始使用生铁和铸造铁的埋弧炉生产。在焦煤稀缺,水力发电既便宜又便宜的地方尤其如此。这些电炉铁工艺使用矿石和助熔剂的组合来生产铁,其成分和金属与炉渣的比例与高炉中的相似。然而,生产铁所消耗的电量约为每净吨2300千瓦时(kWH / NT)。随着对其他​​用途的电力需求的强劲增长,以及高炉中廉价铁的供应,很明显,只有矿石容易获得和水力发电丰富的国家(例如挪威或委内瑞拉)的生产者才有经济能力。电烙铁。尽管随着Tysland-Hole,Strategy-Udy和New Zealand Steel等新工艺的发展,为提高SAF性能而进行的研究仍在继续进行,但这些改进主要集中在装料前对铁氧化物的预还原和预热。这些基于矿石的工艺所用的电仍保持在900 kWH / NT以上。除了少数例外,这些工艺都无法证明与高炉炼钢或冲天炉与铸铁竞争的经济可行性。本文将介绍阿拉巴马州电力公司(APC)的制造铸铁和铁水的工艺。该工艺是基于废料的,生产的铸铁平均碳含量为3.4%,硅含量为2.0%,硫含量为0.06%(重量)。铸铁的平均能耗为474 kWH / NT。由DRI生产的铁水(4.7%C,0.6%Si和0.002%S)的能耗为580 kWH / NT。

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