采用流化床反应器并以水蒸气作为汽化一流化介质,研究了800～950°C内以Fe2O3为载氧体的煤化学链燃烧循环反应特性.实验表明,气态产物CO2的体积浓度(干基)随温度单调递增;CO、CH4的浓度在反应时间内呈单峰特性且随温度单调递减,CH4浓度值高于CO;H2被载氧体完全氧化.载氧体与水煤气化产物在温度高于850°C体现了高的反应活性,CO2干基浓度接近95%.反应器温度900°C时,气态产物CO2体积浓度随循环数而逐渐降低,CO、CH4浓度增加.
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