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Impact of measures adopted to reduce Specific Heat Consumption in Reheating Furnaces of Hot Strip Mill, Roukela Steel Plant, SAIL

机译:SAIL Roukela钢铁厂热轧厂降低炉内比热耗量的措施的影响

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Hot Strip Mill of Rourkela Steel Plant is provided with two Walking Beam Re-heating Furnaces having slab handling capacity of 225 t / hr each. These furnaces were commissioned in the year 1999 and they were designed for cold slab charging. The average Specific Heat Consumption (SHC) of the furnaces was about 376 Mcal /tof cold slab in the year 2000-01 against the international norm of 310 Mcal/t. This paper analyses the impact of different changes adopted like increase in slab thickness, length and width, reduction in mill delays, increase in rolling rate etc. on the reduction in SHC of the furnaces. From the analysis, it was found that every 10 t / mill utilisation hr increase in rolling rate resulted in reduction of SHC by at least 7.7 Mcal /t slab. For increasing the slab rolling rate, the decreasing mill delays (mill unutilised hours/total furnace available hours) played a major role. The mill delays decreased from 37% in 2000-01 to 24% in 2009-10. It was found that for every 1 % reduction in mill delay, the mill rolling rate increases by at least 6t / mill utilisation hr and correspondingly the SHC decreases by at least 4.74 Mcal /t slab. The second most important parameter is the furnace throughput. For every 10t/ mill utilisation hr / furnace increase in furnace throughput, the SHC decreases by at least 12.3 Mcal /t slab. For increasing the furnace throughput, the slab thickness was increased gradually from 206 mm in 200-01 to 218 mm in 2007-08. It was found that for every 1 mm increase in slab thickness, the furnace throughput increases by at least 1.4 t / mill utilisation hr / furnace and the SHC decreases by at least 2 Meal /t slab. However both are not additive as increase in Rolling rate directly influences the Furnace throughput and vice versa. The above measures along with improvement in SOP & SMP resulted in reduction of SHC and the same could be reduced to 344 Mcal /t slab by the year 2011-12.
机译:鲁尔凯拉钢厂的热轧厂配备了两台步进梁式加热炉,每台炉板的处理能力为225吨/小时。这些熔炉于1999年投产,专为冷板坯装料而设计。 2000-01年度,熔炉的平均比热(SHC)约为376 Mcal / tof冷板坯,而国际标准为310 Mcal / t。本文分析了采取的不同变化所产生的影响,如板坯厚度,长度和宽度的增加,轧机延迟的减少,轧制速度的增加等,对降低炉的SHC的影响。从分析中发现,轧制速率每提高10吨/轧钢利用小时,SHC降低至少7.7麦卡尔/吨板坯。为了提高板坯的轧制速度,减少轧机延误(轧机未利用小时/炉子总可用小时)起着重要作用。工厂延误从2000-01年的37%下降到2009-10年的24%。已发现,每延迟1%的轧机延误,轧机轧制速度至少增加6吨/轧机利用小时,相应的SHC降低至少4.74 Mcal / t板坯。第二个最重要的参数是熔炉的生产能力。窑炉产量每增加10吨/小时,窑炉生产能力的降低,SHC至少降低12.3 Mcal / t板坯。为了提高熔炉产量,板坯厚度从200-01的206 mm逐渐增加到2007-08的218 mm。已发现,每增加1 mm的板坯厚度,炉的生产量至少增加1.4 t / mill hr / hr,SHC减少至少2 Meal / t的板坯。然而,两者都不是累加的,因为轧制速率的增加直接影响熔炉的产量,反之亦然。上述措施以及SOP和SMP的改善导致SHC的减少,并且到2011-12年前,其可减少至344 Mcal / t板坯。

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