Effect of Coke Oxidation Kinetics on Mineral Wool Cupola Performance

IF 0.4 4区 材料科学 Q4 MATERIALS SCIENCE, CERAMICS
V. I. Matyukhin, A. V. Matyukhina, S. E. Punenkov
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Abstract

In order to evaluate the effect of impact of the nature of solid fuel on performance indicators of a shaft melting furnace of the cupola type with an internal diameter of 2200 mm and a layer height of 4.5 m, and conditions for its oxidation, the real range of change in the properties of industrial coke batches of various manufacturers is determined (8 varieties) under conditions of non-oxidation heating of coke samples in an argon atmosphere at the rate of 5 deg/min to a temperature of 1000°C and isothermal exposure in an air atmosphere. Operating conditions of the mine unit on these cokes are evaluated with respect to values of specific coke consumption, mineral melt yield, thermal efficiency and changes in conditions for development of heat transfer from gases to materials based upon the ratio of heat capacities of their flows obtained from industrial tests. It is shown that an increase in the complete coke oxidation interval from 7 to 12.5 – 13.0 min will provide a decrease in specific coke consumption from 265 to 225 kg/ton of melt, i.e., by 15.9%, an increase in yield of mineral melt from 25.3 to 30.02%, i.e., by 18.66%, with a decrease in cupola total thermal efficiency from 61.7 to 60.2%, i.e., by 1,5%. For this it is advisable to use coke with maximum heat of combustion. Use of coke mineral raw material during melting, which has a rate of change of sample weight from 5.0 up to 8.0 – 8.5%/min (more active coke), provides a coke minimum specific consumption at the level of 224 kg/ton of melt with a maximum yield of molten smelting product of at least 29.8% of the weight of the initial components with unit thermal efficiency at 61.7%. For this it is necessary to use more active coke with respect to blast oxygen. Heat transfer process conditions from gases to materials during smelting are characterized by low intensity with the lowest ratio of heat capacities of material and gas flows not lower than 0.827 in the range of complete coke oxidation 12.5 – 13.0 min and an average rate of change in sample weight of about 6.0%/min.

Abstract Image

Abstract Image

焦炭氧化动力学对矿棉冲天炉性能的影响
为了评估固体燃料的性质对内径 2200 毫米、层高 4.5 米的冲天炉式竖炉熔化炉性能指标的影响及其氧化条件,在氩气环境中以 5 度/分的速度将焦炭样品加热至 1000°C 的非氧化条件下,以及在空气环境中等温暴露的条件下,确定了不同制造商的工业焦炭批次性能的实际变化范围(8 个品种)。对这些焦炭的矿井装置的运行条件进行了评估,包括焦炭的具体消耗量、矿物熔体产量、热效率以及根据工业试验获得的气体到材料的流动热容量比进行热传导的条件变化。结果表明,焦炭完全氧化间隔从 7 分钟增加到 12.5 - 13.0 分钟,每吨熔体的焦炭消耗量将从 265 公斤减少到 225 公斤,即减少 15.9%,矿物熔体产量从 25.3% 增加到 30.02%,即增加 18.66%,冲天炉总热效率从 61.7% 减少到 60.2%,即减少 1.5%。因此,最好使用燃烧热最大的焦炭。在熔炼过程中,使用样品重量变化率从 5.0 到 8.0 - 8.5%/min 的焦炭矿物原料(活性较高的焦炭),可使焦炭的最小比消耗量达到 224 公斤/吨熔体的水平,熔融冶炼产品的最大产量至少为初始成分重量的 29.8%,单位热效率为 61.7%。为此,必须使用比鼓风氧气更活跃的焦炭。在冶炼过程中,从气体到物料的热传导工艺条件的特点是强度低,在焦炭完全氧化 12.5 - 13.0 分钟的范围内,物料和气体流量的最低热容量比不低于 0.827,样品重量的平均变化率约为 6.0%/分钟。
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来源期刊
Refractories and Industrial Ceramics
Refractories and Industrial Ceramics 工程技术-材料科学:硅酸盐
CiteScore
0.90
自引率
20.00%
发文量
38
审稿时长
6-12 weeks
期刊介绍: Refractories and Industrial Ceramics publishes peer-reviewed articles on the latest developments and discoveries in the field of refractory materials and ceramics, focusing on the practical aspects of their production and use. Topics covered include: Scientific Research; Raw Materials; Production; Equipment; Heat Engineering; Applications.
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