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Modeling of flash smelter operations at the Chagres Smelter

机译:Chagres冶炼厂的闪速冶炼厂操作建模

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摘要

Chagres has operated a Flash Smelting Furnace (FSF) since 1995. Smelter capacity is presently restricted by the Flash Furnace - Waste Heat Boiler (WHB) -Electrostatic Precipitator system. These processes were modeled to assess the factors constituting bottlenecks and predict capacity increases through process and equipment modifications. From a heat balance point of view, the challenge in Flash Furnace operation is to balance heat production of the process and heat extraction capacities of units such as reaction shaft, settler, uptake shaft and waste heat boiler, to achieve adequate operating and product temperatures. The main variables involved are smelting rate, oxygen enrichment, matte grade and supplementary fuel, subject to restrictions. Heat production depends on feed sulfur and iron contents, from several mineralogical species in the concentrate. This paper compares the thermal behavior of the most usual sulfide minerals in the FSF. The interplay between furnace and WHB heat balances is analyzed. To obtain gas temperatures adequate for electrostatic precipitator operation, restriction of heat production in the reaction shaft is the usual solution. However, uncompensated heat losses in the FSF settler may require higher fuel usage, with higher heat loads on the WHB. The present modeling work addresses the study of these effects.
机译:Chagres自1995年以来一直使用闪速熔炼炉(FSF)。目前,熔炉的生产能力受到闪速熔炉-废热锅炉(WHB)-静电除尘器系统的限制。对这些过程进行建模,以评估构成瓶颈的因素并通过过程和设备修改来预测产能的增加。从热平衡的观点来看,闪蒸炉操作中的挑战是平衡过程的热量产生和反应竖井,沉降器,吸收竖井和废热锅炉等装置的吸热能力,以实现足够的运转温度和产品温度。所涉及的主要变量是冶炼速度,氧气富集度,磨砂等级和辅助燃料,但有限制。热量的产生取决于进料中硫和铁的含量,这些硫和铁的含量来自精矿中的几种矿物。本文比较了FSF中最常见的硫化物矿物的热行为。分析了熔炉和WHB热平衡之间的相互作用。为了获得足以使静电除尘器运行的气体温度,通常的解决方案是限制反应竖井中的热量产生。但是,FSF沉降器中未补偿的热量损失可能需要使用更多的燃料,而WHB上的热量会更高。当前的建模工作解决了对这些影响的研究。

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