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《钢铁冶炼》2013,40(6):433-438
AbstractIn this study, the effect of MgO content in slag on the phosphorus distribution ratios, and the equilibrium solubility of MgO in slag during converter steelmaking were analysed using the modified Kozheurov regular solution model and the thermodynamic package FactSage. Thermodynamic analysis shows that the MgO content in the final slag should be greater than 5% to saturate the slag with MgO and minimise the chemical wear of the refractory lining. However, the phosphorus distribution ratio decreases dramatically with increasing MgO. Industrial tests were performed using an 80-t top-and-bottom combined blown converter showed that the average phosphorus distribution ratio reduces significantly from 120.7 to 75.7 when the average MgO content in the final slag increases from 7.0 to 9.8%, due to thermodynamics and kinetics reasons. By optimizing the MgO content between 6 and 8% dephosphorisation and refractory wear are optimised. 相似文献
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随着超低碳、超低磷钢种冶炼的增多,济钢复吹转炉终点氧含量大幅提高,严重侵蚀了转炉炉衬。从高氧化性炉渣对炉衬的侵蚀机理入手,提出了兼顾溅渣层和炉底的溅渣工艺,介绍了超低碳、超低磷钢溅渣护炉工艺参数的优化及取得的效果。 相似文献
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针对转炉炉渣MgO含量偏低的现象,对转炉使用溅渣镁球代替轻烧白云石造渣技术,合理控制溅渣镁球的加入量,达到降低终渣FeO、提高渣中MgO来迅速降低炉渣过热度等目的,从而可以缩短溅渣时间,提高溅渣层的抗侵蚀能力,最大限度发挥溅渣护炉效果,延长补炉间隔时间,节约耐火材料,提高生产作业率,并降低炼钢的冶炼成本。 相似文献
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溅渣护炉工艺是近期发展起来的一项新技术,该工艺设备简单,投资少,收效快,操作方便,可大幅度提高衬寿命,进而提高炉龄次数,介绍了溅渣护炉工艺原理,有关参数及经济效益。 相似文献
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通过分析了水钢100 t顶底复吹转炉炉衬的损坏机理和影响炉渣熔化性能的因素,得出每1%V2O5降低炉渣熔化温度27℃,每增加1%TiO2含量,炉渣半球温度约降低5℃,当炉渣TFe含量在20%以上时,炉渣熔化温度在1 320~1 395℃。通过采取铁水捞渣工艺;建立转炉热平衡操作模式,提高拉碳率;铁水Si在0.6%~0.8%时,采用单渣操作,铁水Si>0.8%时,采用双渣操作;建立转炉最佳炉型及控制措施;优化钢水温度制度和优化脱氧合金化制度,降低出钢温度;在补吹提枪前加入适量焦丁,确保冶炼终点炉渣中FeO保持较低含量,提高溅渣护炉效果等工艺措施,结果使转炉炼钢的耐火材料消耗降到8.75 kg/t钢,转炉炉龄达到29 336炉。 相似文献
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京唐公司炼钢系统铁水转炉预脱磷及“全三脱”铁水少渣冶炼工艺不断进行技术优化,脱磷转炉通过优化废钢尺寸、底吹枪数量和排布,半钢脱磷率可达到70%;铁水经过脱磷转炉脱硅、脱磷后,温度和磷质量分数更加稳定,为脱碳转炉少渣冶炼、自动化炼钢终点双命中率的提高提供了先决条件;脱碳转炉通过采用留渣操作、少渣冶炼技术、溅渣护炉技术后,自动化命中率达到90%以上,炉龄达到7 000炉以上;炼钢车间内渣钢、除尘灰、氧化铁皮等含铁物料实现了自循环消耗。采用“全三脱”铁水冶炼工艺,钢种质量进一步提高,超低磷与超低硫钢中(S+P+N)元素质量分数可稳定控制在0.009 5%以下。 相似文献
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A slag layer is formed when slag is splashed onto refractory lining in BOF slag splashing process. The melting temperature of the slag layer and the adhesion of the slag layer to the lining refractory have an important effect on slag splashing and BOF lining life. This study investigates the adhesive behaviour of slag with different composition to lining refractories. It is shown that the slag can adhere to MgO particles in MgO‐C bricks well and no reaction is found between the MgO particles and the slag layer, but a gas gap exists at the interface between the slag layer and the MgO‐C matrix and there are iron granules within the slag layer, when the FeO content in the slag is high. The adhesion of the slag layer to the lining refractory can be improved with decreasing FeO content in the slag and lower carbon content in the MgO‐C bricks. BOF refractory lining life can be greatly increased due to better adhesion, high melting temperature, and stronger wear‐resistance of the slag layer. 相似文献
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转炉冶炼过程金属熔体的喷溅对于转炉反应器的性能有重要影响。氧枪作为氧气射流的产生及控制单元,决定了转炉吹炼过程熔体的喷溅行为。通过水模型试验,研究了漩流氧枪转炉冶炼过程熔体的喷溅,考察了氧枪喷孔扭转角设计及操作参数下熔体喷溅速率和喷溅的空间分布规律,基于此,分析了漩流氧枪对转炉反应器性能的影响。结果表明,相比于传统氧枪吹炼,漩流氧枪吹炼时熔体喷溅速率降低,喷溅高度下降,喷溅在径向空间分布趋于均匀,且随着喷孔扭转角的增大,该分布规律变化更为显著,扭转角大于20°时,喷溅到炉口及炉外的熔体降为零。漩流氧枪吹炼时,喷溅速率及喷溅量在不同径向和高度位置处分布随着顶吹气量的增大而增大,受枪位的影响规律与扭转角有关。 相似文献
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西钢120t转炉采用科学设计北方烘炉方案,采取分区段控制溅渣操作要点,严格落实操作工艺要求和步骤,实现北方钢厂大型转炉第一代炉役接近20000次的突破,取得良好的效果。 相似文献
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简介了济钢第一炼钢厂在炉龄提高后的炉型控制状况;重点针对溅渣后炉型的变化,优化了溅渣护炉和砌炉工艺,改进了炉渣性质,进而提高了溅渣护炉效果和保持了合理炉型,保证了生产的稳定运行。该厂控制炉型的实践对炼钢生产有一定的指导意义。 相似文献
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Timo Matti Juhani Fabritius Petri Tapani Mure Pentti Antero Kupari Veikko Antero Juntunen Jouko Juhani Hrkki 《国际钢铁研究》2001,72(7):237-244
Traditionally, in stainless steelmaking converters, oxygen has been blown by a one‐hole lance (1 HL) and sidewall tuyères. In order to reduce the tap‐to‐tap time, the multi‐hole lance has been used for oxygen blowing. The aim of this work was to develop blowing practise for a multi‐hole lance to reduce the tap‐to‐tap time and minimise metal splashing and spitting in the sidewall blowing converter (chromium converter). In the chromium converter the chemical energy of liquid ferrochrome (which contains 4 % silicon and 7 % carbon) is utilised for scrap melting by oxidising the silicon and the part of carbon. The research has been made by a dynamically scaled water model and full‐scale converter. Used parameters were the gas flowrate from sidewall tuyères and lance, lance height, charge weight and position of multi‐hole lance. Splashing has been measured during blowing from walls (splashing) and mouth of the converter model (spitting). The model tests indicated less splashing and spitting by the three‐hole lance (3 HL) than traditional 1 HL. The 1 HL caused strong skulling of the converter cone. By 3 HL blowing the position of the lance has a remarkable effect on the direction and the amount of splashing and lance life. Because of hot metal‐slag splashes, the life time of the 3 HL was halved by position 1 (compared to 1 HL). With the lance position 2 the splashing decreased by approx. 50% in model tests and lance life time increased by ~ 50% (compared to 1 HL) in the full‐scale converter. The model agreed well with the full‐scale converter. According to the process tests, the nominal productivity of the chromium converter has increased 15 % and depending on the refining practise and the silicon content of ferrochromium the lining life has increased 20 ‐ 30 %. In the future the multi‐hole lance will be tested in the AOD vessel. 相似文献