Chemical looping oxidative dehydrogenation of ethane over Fe-Co/HZSM-5 redox catalyst: role of acidity and dual-metal oxides synergy
编号:95 稿件编号:164 访问权限:仅限参会人 更新:2023-04-03 18:49:19 浏览:359次 口头报告

报告开始:2021年08月10日 01:00 (Asia/Shanghai)

报告时间:15min

所在会议:[P] 大会报告 » [2] 分会场一:反应器设计及系统优化

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摘要
Chemical looping oxidative dehydrogenation (CL-ODH) has been extensively investigated as a green strategy for light olefins production from alkanes/naphtha without thermodynamic equilibrium constraints. However, achieving high ethylene selectivity as well as promising ethane conversion at relatively low-temperature (≤ 600 °C) remains challenging so far in chemical looping oxidative dehydrogenation (CL-ODH) of ethane. Dual-metal oxides (especially non-expensive ones) supported zeolite may possess promising ethane ODH performance due to the tunable acidity and redox property, which has rarely been investigated under the context of CL-ODH. Herein, we show that Fe-Co dual-metal oxides supported HZSM-5 can be used as appropriate redox catalyst for CL-ODH of ethane. By adjusting the Fe: Co ratio in the mixed oxides as well as the Si: Al ratio in the HZSM-5 support, the synergy of dual-metal oxides and the role of sample acidity in ethane ODH reaction were systematically investigated. In addition, the effects of reaction temperature and gas hourly space velocities (GHSV) on the ethane ODH performance of 8Fe-2Co/HZ5(200) were investigated. As it turned out, the best-performing sample, i.e., 8Fe-2Co/HZ5(200), demonstrated ~87% ethylene selectivity at 23% ethane conversion under reaction temperature of 600 °C and the GHSV of 4800 mL·h-1·g-1. The stable ethane ODH performance achieved over 100 redox cycles without coking further indicated the feasibility of its utilization in CL-ODH. Physicochemical characterization techniques including XRD, SEM, TEM-EDS, NH3-TPD, H2-TPR, XPS, and C2H6-TPR were used to elucidate the structure-function relationship of the redox catalysts. Comparison testing and physicochemical characterization results showed that both sample acidity and dual-metal oxides synergy are pivotal for ethane ODH to yield ethylene, in which dual-metal oxides are responsible for low-temperature ethane activation while sample acidity is critical for ethylene selectivity as well as activity. The present work demonstrates the feasibility of using dual-metal oxides supported HZSM-5 for low-temperature CL-ODH of ethane, and provides sights for redox catalyst design to achieve a good balance between sample activity and selectivity.
关键字
Oxidative dehydrogenation, chemical looping, ethylene production, dual-metal oxides, HZSM-5
报告人
张东红
在读博士 武汉大学

稿件作者
张东红 武汉大学
田鑫 武汉大学
张阳 武汉大学
定明月 武汉大学
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