生物质化学链燃烧中燃烧特性与气固流动特性的CFD模拟研究OA
Computational fluid dynamics investigation on combustion and gas-solid flow characteristics in biomass chemical looping combustion
基于计算流体力学方法,采用双流体模型耦合化学反应动力学,模拟了四种典型生物质原料(松木锯末、玉米秸秆、稻草和杏仁壳)热解气与三种载氧体(Fe2O3、CuO及复合载氧体CuFe2O4)在化学链燃烧燃料反应器内的气固两相流动及燃烧特性,进一步探究了反应温度对燃烧过程的影响规律.结果表明,不同生物质原料在热解阶段释放的可燃气体成分存在显著差异:松木锯末在热解过程中的可燃气体含量较高(33.38%CO和29.22%H2),略低于玉米秸秆和杏仁壳的相应气体含量,但远高于稻草的相应气体含量;在燃料反应器中燃烧反应达到稳态后,松木锯末的可燃气体含量(8%~12%)远低于玉米秸秆和杏仁的相应气体含量,略高于稻草的相应气体含量.综合考虑燃烧稳定性与燃料转化率,松木锯末表现出最佳的燃烧性能,其最佳反应温度在880 ℃左右.此外,反应温度对不同载氧体性能的影响具有明显差异:CuO在高温下转化率衰减迅速,而CuFe2O4的转化率随温度升高而增加.就CO转化率而言,CuFe2O4显著优于Fe2O3,略低于CuO;就H2转化率而言,CuFe2O4介于Fe2O3与CuO之间,且在760 ℃~920 ℃内CO和H2的转化率均能保持稳定;CuFe2O4综合反应性能优于单一金属氧化物(CuO和Fe2O3)综合反应性能.
Computational fluid dynamics(CFD)simulations were conducted using a two-fluid model coupled with chemical reaction kinetics to investigate the gas-solid two-phase flow and combustion characteristics of pyrolysis gases from four typical biomass feedstocks(pine sawdust,corn straw,rice straw and almond shell)in the presence of three oxygen carriers(Fe2O3,CuO and CuFe2O4)in a chemical looping combustion(CLC)fuel reactor.The effects of reaction temperature on the combustion process were further explored.The results indicate that there are significant differences in the combustible gas components released by different biomass feedstocks during the pyrolysis stage.Pine sawdust produces relatively high CO and H2 contents(33.38%and 29.22%,respectively),which are slightly lower than the corresponding values for corn stalk and almond shell,but much higher than those of rice straw.After the combustion reaches a steady state,the residual combustible-gas content for pine sawdust(8%-12%)is much lower than that for corn stalk and almond shell,but slightly higher than that for rice straw.Considering both combustion stability and fuel conversion rate,pine sawdust exhibits the best combustion performance with an optimal reaction temperature of approximately 880 ℃.In addition,the effects of reaction temperature on the performance of different oxygen carriers differ markedly.The conversion rate of CuO decreases rapidly at high temperatures,while that of CuFe2O4 increases with rising temperature.The CO conversion rate of CuFe2O4 is significantly higher than that of Fe2O3 but slightly lower than that of CuO.Its H2 conversion rate is between that of Fe2O3 and CuO.Furthermore,CuFe2O4 maintains stable conversion rates for both CO and H 2 over the range of 760 ℃-920 ℃.Thus,the overall reaction performance of CuFe2O4 is superior to that of single-metal oxides(CuO and Fe2O3).
赵博贤;吕雪;马效彪;刘晶;杨应举;王思路
华中科技大学煤燃烧与低碳利用全国重点实验室,430074武汉华中科技大学煤燃烧与低碳利用全国重点实验室,430074武汉华中科技大学煤燃烧与低碳利用全国重点实验室,430074武汉华中科技大学煤燃烧与低碳利用全国重点实验室,430074武汉华中科技大学煤燃烧与低碳利用全国重点实验室,430074武汉华中科技大学煤燃烧与低碳利用全国重点实验室,430074武汉
能源科技
生物质化学链燃烧载氧体CFD模拟气固流动特性
biomass-fueled chemical loopingcombustionoxygen carrierCFD simulationgas-solid flow characteristics
《煤炭转化》 2026 (4)
35-43,9
国家重点研发计划项目(2024YFE0101400)
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