Steelmaking using an Electric Arc Furnace (EAF) has gained more interest in recent years, due to the low capital and operating cost; and its flexibility in the use of raw materials (i.e. scrap). Depending on the cost and availability, anthracite and metallurgical coke are among the conventionally injected materials used for foaming in EAF steelmaking. Considering the energy and green house gas emissions requirements, alternative carbon sources are put on the spot to replace, at least partially, the conventional materials, i.e.. waste materials such as Rubber and polypropylene (PP) plastics may react with gas and slag phases resulting in devolatilization, combustion and iron oxide reduction reactions. In the present study, the conventional material investigated was metallurgical coke which was blended with different proportions of rubber and PP. Metallurgical coke, Rubber-coke blends and PP coke blends were combusted in a drop tube furnace (DTF) at 1200 ºC under 20%O2 and 80% N2 gas mixture. Subsequently, the residual materials were put in contact with two EAF iron oxide rich slags and their interfacial reactions and phenomena have been studied at 1450-1550ºC in a horizontal tube furnace under inert atmosphere (1l/min Ar) with off gases measured using an IR analyser. The initial devolatilization and the subsequent step of combustion of these samples are considered in a Drop Tube Furnace (DTF) and in a Thermogravimetric Analyser (TGA), respectively, while the sessile drop approach investigated the interfacial reactions taking place in the slag/carbon region. The gas phase studies showed a reactive rubber-coke residue with an improved surface area resulted from volatile matter removal. The rate of devolatilization appears to improve the coke-rubber burnout as well as its foaming behavior when put in contact with an iron oxide rich slag. However, a higher rate of devolatilization, as seen in PP-coke blends shows a fragmented particle which affects the combustion while less volatiles are available to sustain subsequent reactions in the slag phase.Off gas analyses following the carbon/slag interfacial reactions have been measured for all the carbonaceous materials and significantly different gas concentrations have been observed. The CO and CO2 emissions from metallurgical coke showed lower concentrations in comparison to that from the coke-rubber and coke-PP blends. At 1550º C, both slags were non-wetting in the initial stage of reaction dictated by the chemical reaction and gas evolution. A slower rate of chemical reaction is seen when coke reacted with the EAF slag, while the rubber blends showed a faster reduction leading to a further drop in the contact angle θ. Independent of the carbon material used as a substrate, the final stage of reaction reveals comparable contact angles due to similar extents of reduction and Fe deposition at the interface. Extensive FeO reduction followed when the EAF slag reacted with the carbonaceous materials. Coke and its low activation energy value correlates with less gas and thus less stirring in the slag and mass transfer in the liquid becomes an important rate limiting step. With increasing proportion of rubber in the blend, moving the process towards mixed controlled in which chemical control becomes important as seen in the trends in the activation energy values. Therefore a mixed controlled process limits the FeO reduction reaction for coke and coke-rubber blends. Higher gas entrapment in the slag was observed when rubber partially replaced coke. The lower devolatilization rates seen in rubber blends compared to PP blends allows the formation of a highly porous particle, promoting gasification and allowing more gases to be trapped in the slag phase compared to PP blends. Optimization between the two phenomena, reduction and foaming is required for improved EAF process performance. Industrial trials using rubber as partial carbon source in EAF steelmaking resulted in decreased specific energy consumption compared to coke alone. This study highlights significant differences in the carbon/slag interactions of coke/rubber blends with EAF slag, compared to interaction of coke with the same slag and enhances the possibility of utilizing polymeric wastes in blends with conventional materials, such as coke, in EAF steelmaking.
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机译:近年来,由于资本和运营成本低廉,使用电弧炉(EAF)进行炼钢越来越引起人们的兴趣。以及在使用原材料(即废料)方面的灵活性。取决于成本和可获得性,无烟煤和冶金焦是EAF炼钢中用于发泡的常规注入材料。考虑到能源和温室气体排放的要求,替代碳源被当场替代,至少部分替代了传统材料,即诸如橡胶和聚丙烯(PP)塑料之类的废料可能会与气相和炉渣相反应。在脱挥发分,燃烧和氧化铁还原反应中。在本研究中,所研究的常规材料是冶金焦炭,其与不同比例的橡胶和PP混合。将冶金焦炭,橡胶焦炭混合物和PP焦炭混合物在滴管炉(DTF)中于1200℃,20%O2和80%N2气体混合物中燃烧。随后,将残余材料与两种EAF富氧化铁炉渣接触,并在1450-1550ºC的水平管式炉中在惰性气氛(1l / min Ar)下研究了它们的界面反应和现象,并使用红外测量了废气分析器。这些样品的初始脱挥发分和随后的燃烧步骤分别在滴管炉(DTF)和热重分析仪(TGA)中进行了研究,而无滴法研究了在炉渣/碳区中发生的界面反应。气相研究表明,由于去除了挥发性物质,反应性橡胶焦渣的表面积得到了改善。当与富铁氧化物的炉渣接触时,脱挥发分的速率似乎改善了焦炭橡胶的燃尽及其起泡行为。但是,PP焦炭共混物中的挥发度较高,表明碎片会影响燃烧,而挥发物较少以维持炉渣相继的反应。对碳/炉渣界面反应后的废气进行了测量对于所有含碳物质,已经观察到明显不同的气体浓度。与焦炭-橡胶和焦炭-PP混合物相比,冶金焦产生的CO和CO2排放浓度较低。在1550°C时,由化学反应和气体逸出所决定的反应初期,两种炉渣均未润湿。当焦炭与EAF炉渣反应时,发现化学反应速度较慢,而橡胶混合物的还原速度更快,导致接触角θ进一步降低。不依赖于用作基材的碳材料,反应的最后阶段显示出可比的接触角,这归因于相似的还原程度和界面处的Fe沉积。当EAF炉渣与碳质材料反应后,FeO大量还原。焦炭及其低活化能值与较少的气体相关,因此炉渣中的搅拌较少,液体中的传质成为重要的限速步骤。随着橡胶在共混物中的比例增加,使过程朝着混合控制的方向发展,如活化能值趋势所示,化学控制变得很重要。因此,混合控制过程限制了焦炭和焦炭橡胶混合物的FeO还原反应。当橡胶部分替代焦炭时,观察到渣中有更高的气体截留率。与PP共混物相比,橡胶共混物中较低的脱挥发分速率可形成高度多孔的颗粒,从而促进气化,并使更多的气体被截留在炉渣相中。为了改善EAF工艺性能,需要在还原和发泡这两种现象之间进行优化。与仅使用焦炭相比,在EAF炼钢中使用橡胶作为部分碳源的工业试验降低了单位能耗。这项研究突显了与焦炭与相同炉渣的相互作用相比,焦炭/橡胶混合物与EAF炉渣的碳/渣相互作用之间存在显着差异,并增加了在电炉炼钢中利用聚合物废物与常规材料(如焦炭)的混合物中利用聚合物废物的可能性。 。
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