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Effect of Gas Velocity Distribution on Heat Recovery Process in Packed Bed of Plate-Shaped Slag

机译:气体流速分布对板状炉渣填充床热回收过程的影响

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A new twin-roll continuous slag solidification process and heat recovery process from a slag packed bed was developed for utilization of the waste heat of steelmaking slag. Plate-shaped slag with the thickness about 7 mm was successfully produced in a pilot plant, and the sensible heat of the slag was recovered by blowing air into the slag chamber. However, the gas distribution inside the slag packed bed was unclear because of the unique shape of the slag plates, and this remained a concern for further scale-up designing of the slag chamber. Therefore, in order to estimate the gas distribution in the packed bed, a simple computational fluid dynamics (CFD) model which considers the wall effect around the inner wall of the chamber was developed, and this model was fitted to the results of laboratory-scale velocity distribution measurements. The results showed that the gas velocity distribution was properly estimated, and the intensity of the wall effect was similar in both cases. As the next step, the gas velocity distribution and its effect on the slag heat recovery process in a pilot-scale slag chamber were evaluated with the assistance of the CFD simulation model. The simulation results were compared with the measured data obtained in a pilot-scale test, and as the result, a similar wall effect was also observed in the pilot-scale chamber. However, the intensity of the wall effect was limited enough to prevent serious deterioration of the uniformity of the gas distribution.
机译:为了利用炼钢炉渣的余热,开发了一种新型的双辊连续炉渣凝固工艺和炉渣填充床的热回收工艺。在中试工厂成功生产出厚度约7毫米的板状炉渣,并通过向炉渣室吹入空气来回收炉渣的显热。然而,由于炉渣板的独特形状,炉渣填充床内部的气体分布尚不清楚,这仍然是进一步扩大炉渣室设计的关注点。因此,为了估算填充床中的气体分布,建立了一个考虑腔室内壁周围壁效应的简单计算流体动力学(CFD)模型,并将该模型与实验室规模的结果进行了拟合。速度分布测量。结果表明,在两种情况下,气体速度分布都得到了正确估计,并且壁效应的强度相似。下一步,借助CFD模拟模型评估了中试炉渣室内的气体速度分布及其对炉渣热回收过程的影响。将模拟结果与通过中试测试获得的测量数据进行比较,结果在中试室中也观察到了类似的壁效应。但是,壁效应的强度受到足够的限制,以防止气体分布均匀性的严重恶化。

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