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Modelling and simulation of steel reheating processes under oxy-fuel combustion conditions - Technical and environmental perspectives

机译:含氧燃料燃烧条件下钢的加热过程的建模和仿真-技术和环境观点

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This paper investigates the impact of flameless oxy-fuel combustion on the thermal performance of a pilot-scale steel reheating furnace. A comprehensive mathematical model, based on the zone method of radiation analysis, was developed, which takes into account the non-grey behaviour of the furnace atmosphere under oxy-fuel combustion conditions. The model was subsequently used to simulate the temperature profile of an instrumented slab used in the experiment. The results showed that the predicted slab temperature profile along the furnace is in good agreement with measurement. However the model over predicted the absolute slab temperatures due to the influence of formation of oxide scales on the slab surface, which was not taken into account in the current model. When compared to air-fuel combustion simulation, the results of oxy-fuel combustion also indicated a marked improvement in the furnace specific fuel consumption (approximately 16%). This was mainly due to the enhanced radiative properties of the furnace atmosphere and reduced exhaust energy losses as the result of less dilution effect from nitrogen. This resulted in reduction in the overall heating time by approximately 14 min. Furthermore, if the economics of carbon capture is taken into consideration, theoretically, the energy consumption per kilogram of CO2 captured can be reduced from 3.5 to 4.2 MJ kg(-1) to 0.96 MJ kg(-1). In conclusion, the current studies support the view that oxy-fuel combustion retrofitting to reheating furnaces is a promising option, both from a technical and from an environmental point of view. (C) 2019 Elsevier Ltd. All rights reserved.
机译:本文研究了无焰含氧燃料燃烧对中试规模的钢制加热炉热性能的影响。建立了基于辐射分析区域法的综合数学模型,该模型考虑了氧-燃料燃烧条件下炉内气氛的非灰色行为。该模型随后用于模拟实验中使用的仪器平板的温度曲线。结果表明,沿炉膛的板坯温度预测曲线与测量值吻合良好。但是,由于板坯表面氧化皮形成的影响,该模型过高地预测了板坯的绝对温度,当前模型中未将其考虑在内。当与空气燃料燃烧模拟进行比较时,含氧燃料燃烧的结果还表明,窑炉的单位燃料消耗量显着提高(约16%)。这主要归因于由于氮稀释作用较小而提高了炉内气氛的辐射性能并减少了排气能量损失。这导致整体加热时间减少了大约14分钟。此外,如果考虑碳捕集的经济性,从理论上讲,每千克捕集的二氧化碳的能耗可以从3.5降低到4.2 MJ kg(-1)到0.96 MJ kg(-1)。总之,从技术和环境的角度来看,当前的研究都支持这样一种观点,即将氧气燃料燃烧改造为再热炉是一种有前途的选择。 (C)2019 Elsevier Ltd.保留所有权利。

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