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氧氣高爐回旋區內煤粉燃燒行為的數值模擬

Numerical simulation of pulverized coal combustion in the raceway of an oxygen blast furnace

  • 摘要: 爐頂煤氣循環-氧氣鼓風高爐煉鐵新技術的工藝特點決定了煤粉在其回旋區內的燃燒條件與傳統高爐相比將發生很大變化.本文建立了氧氣高爐直吹管—風口—回旋區下部煤粉流動和燃燒的數學模型,研究了入口布置方式、氧含量、循環煤氣溫度以及H2O和CO2含量對煤粉燃燒的影響.模擬結果表明:三種引入方式中,假想的循環煤氣和氧氣混合進入方式明顯優于循環煤氣和氧氣單獨進入方式.當氧的體積分數由80%增加到90%,相應的煤粉燃盡率由87.525%提高到93.402%.循環煤氣溫度對煤粉燃盡率的影響并不顯著.循環煤氣中H2O和CO2的體積分數提高5%,風口軸線上氣體的最高溫度分別降低124 K和113 K.

     

    Abstract: The technological characteristics of a top gas recycling-oxygen blast furnace determine that in comparison with a traditional blast furnace the combustion condition of pulverized coal in the raceway has great changes. A mathematical model of pulverized coal flow and combustion in the blowpipe-tuyere-raceway bottom is developed in this paper. The influences of entry modes,oxygen enrichment,recycling gas temperature,H2O and CO2 contents on the burnout of pulverized coal are investigated by this model. The results indicate that an entry mode with the premixing of recycling gas and oxygen is obviously better than two other modes with recycling gas and oxygen entering alone. When the oxygen content changes from 80% to 90% the coal burnout increases from 87.525% to 93.402%. The effect of recycling gas temperature is not significant. The maximum gas temperature along the tuyere axis decreases by 124 K with the increasing of H2O content in the recycling gas by 5%,and it drops by 113 K for CO2.

     

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