首页|生物质化学链气化制富氢合成气的研究

生物质化学链气化制富氢合成气的研究

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本文通过溶胶凝胶法制备了 Ca2Fe2O5氧载体用于生物质化学链气化制备富氢合成气研究。结果表明,相比于生物质常规的热解和水蒸气气化,采用Ca2Fe2O5作为氧载体进行化学链气化时水蒸气和氧载体的协同作用大大提高了 H2产率和碳转化率;不同氧载体实验和热力学分析结果对比凸显了 Ca2Fe2O5氧载体优异的反应特性;通过对反应工况进行优化得出最佳反应条件为气化温度850℃、水蒸气浓度30%和氧燃比0。2,该工况下H2产率和总气体产率为0。91 m3/kg和1。83 m3/kg,H2/CO比接近3;最后,10次循环实验以及氧载体表征结果表明Ca2Fe2O5氧载体的循环稳定性良好,在10次循环过程保持相对稳定的气体产率,且氧载体晶相和微观形貌并无较大改变。
Study on Chemical Looping Gasification of Biomass for Hydrogen-rich Syngas Production
In this paper,Ca2Fe2O5 oxygen carrier was prepared by sol-gel method for the produc-tion of hydrogen-rich syngas from chemical looping gasification of biomass.The results show that compared with the conventional pyrolysis and steam gasification of biomass,the synergistic effect of steam and oxygen carrier greatly improves the H2 yield and carbon conversion rate when Ca2Fe2O5 is used as oxygen carrier.The comparison of different oxygen carrier and thermodynamic analysis highlights the excellent reaction characteristics of Ca2Fe2O5 oxygen carrier.By optimizing the reac-tion conditions,the optimum reaction conditions were obtained as follows:gasification temperature 850℃,steam concentration 30%and oxygen-fuel ratio 0.2.Under this condition,the H2 yield and total gas yield were 0.91 m3/kg and 1.83 m3/kg,respectively,and the H2/CO ratio was close to 3.Finally,10 cycles of experiments and oxygen carrier characterization results show that the Ca2Fe2O5 oxygen carrier has good cycle stability,where the crystal phase and microstructure of the oxygen carrier have almost no change.

chemical looping gasificationoxygen carrierhydrogen-rich Syngas

王潘磊、徐祖伟、赵海波

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华中科技大学煤燃烧与低碳利用全国重点实验室,武汉 430074

化学链气化 氧载体 富氢合成气

2024

工程热物理学报
中国工程热物理学会 中国科学院工程热物理研究所

工程热物理学报

CSTPCD北大核心
影响因子:0.4
ISSN:0253-231X
年,卷(期):2024.45(12)