回转窑内煤粉−烟气混合燃烧特性

Characteristics of coal powder-gas mixture combustion in rotary kiln

  • 摘要: 为了解决矿热炉冶炼过程中存在排放大量高温烟气造成能源浪费、环境污染的问题,提出回收矿热炉烟气中CO等可燃成分作为回转窑辅助燃料的工艺,并设计了一款新型5通道燃烧器,以此实现回转窑内煤粉−烟气燃料的混合燃烧,利用CFD(Computational Fluid Dynamics)理论,建立了煤粉−烟气混合燃烧的数学模型,数值模拟了回转窑中气固两相燃料混合燃烧的过程,分析了气固两相燃料不同混合比时,回转窑内温度场、燃烧特性(组分场)以及NOx的变化情况。结果表明:回转窑内存在内外循环区,可加速燃料与空气的混合,提高窑内换热量。烟气燃料的加入有助于改善煤粉的燃烧特性,当烟气燃料发热量占总发热量的比值由20%增至40%,窑内温度场均呈现轴对称分布,黑火头的长度逐渐由4.51 m减小至2.32 m,火焰峰值温度逐渐降低,挥发分的燃烧速率逐渐由4.21 mol/(m3·s)提高至7.33 mol/(m3·s),炉窑出口处NOx的质量浓度逐渐降低,由1 013 mg/m3下降至677 mg/m3。当烟气燃料发热量占总发热量的比值由20%增至30%时,火焰形状由“球团状”逐渐变长变窄,煤粉的燃烧位置由X=4.68 m前移至X=2.26 m,回转窑焙烧带长度由18.50 m增至20.50 m。但随着烟气燃料发热量占总发热量的比值由30%增至40%时,火焰形状逐渐向“棒槌状”转变,煤粉的燃烧位置无明显变化,焙烧带长度由20.50 m降至16.43 m。综合分析焙烧带长度、燃料燃烧等特性,确定当烟气燃料发热量占总发热量的比值为30%时为最佳掺混比。

     

    Abstract: Currently, a large amount of high temperature furnace gas is discharged in the smelting process of electric furnace, which causes energy waste and environmental pollution. The process of recovering combustible components such as CO from electric furnace flue gas as auxiliary fuel for rotary kilns was proposed. A new five-channel burner was designed to realize the mixed combustion of pulverized coal and electric furnace flue gas in rotary kilns. Afterwards, CFD(Computational Fluid Dynamics) theory was used to establish the mathematically model of pulverized coal and electric furnace flue gas co-combustion. The process of gas-solid two-phase fuel co-combustion in a rotary kiln was numerically simulated. The temperature fields, combustion characteristics and NOx changes in rotary kilns were analyzed under different electric furnace flue gas mixing ratios. The results show that the inner and outer circulation zones can be observed in the rotary kiln, which can accelerate the mixing of fuel and air. As a result, the amount of heat transfer in the rotary kiln is increased. The addition of electric furnace flue gas helps to improve the combustion characteristics of pulverized coal. When the electric furnace flue gas ratio increases from 20% to 40%, the temperature distribution inside the rotary kiln exhibit axisymmetry, and the length of the black flame gradually decreased from 4.51 m to 2.32 m. Then the peak flame temperature gradually decreases, the combustion rate of volatile components gradually increases from 4.21 mol/(m3·s) to 7.33 mol/(m3·s). Besides, the concentration of NOx at the rotary kiln outlet gradually decreases from 1 013 mg/m3 to 677 mg/m3. With increasing the electric furnace flue gas ratio from 20% to 30%, the flame shape gradually elongates and narrows from a “pellet”, the combustion position of pulverized coal moves forward from X=4.68 m to X=2.26 m, and the length of rotary kiln roasting zone increases from 18.50 m to 20.50 m. However, with increasing the electric furnace flue gas ratio from 30% to 40%, the flame gradually shift to a “wooden-club shaped”, there is no significant change of the combustion position of pulverized coal. Besides, the length of roasting zone correspondingly decreases from 20.50 m to 16.43 m. By comprehensively analyzing the length of the roasting zone and the characteristics of fuel co-combustion, it is determined that the optimal electric furnace flue gas ratio is 30%.

     

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