Volume 8 Issue 3
您当前的位置:首页 > 期刊文章 > 过刊浏览 > Volume 8 (2010) > Volume 8 Issue 3
Tang, Y., Chen, L., Wang, M., Li, J., & Lu, Y. (2010). Microfibrous entrapped ZnO-CaO/Al2O3 for high efficiency hydrogen production via methanol steam reforming. Particuology, 8(3), 225-230. https://doi.org/10.1016/j.partic.2010.03.010
Microfibrous entrapped ZnO-CaO/Al2O3 for high efficiency hydrogen production via methanol steam reforming
Ying Tang, Li Chen, Miaomiao Wang, Jianfeng Li, Yong Lu *
Shanghai Key Laboratory of Green Chemistry and Chemical Processes, Department of Chemistry, East China Normal University, Shanghai 200062, China
10.1016/j.partic.2010.03.010
Volume 8, Issue 3, June 2010, Pages 225-230
Received 15 January 2009, Accepted 16 May 2009, Available online 1 April 2010.
E-mail: ylu@chem.ecnu.edu.cn

Highlights
Abstract

Sinter-locked microfibrous networks consisting of ∼3 vol.% of 8 μm (dia.) nickel microfibers have been utilized to entrap ∼30 vol.% of 100–200 μm dia. porous Al2O3. ZnO and CaO were then highly dispersed onto the pore surface of the entrapped Al2O3 by the incipient wetness impregnation method. Due to the unique combination of surface area, pore size/particle size, thermal conductivity, and void volume, the resulting microfibrous catalyst composites provided significant improvement of catalytic bed reactivity and utilization efficiency when used in methanol steam reforming. Roughly 260 mL/min of reformate, comprising >70% H2, <5% CO and trace CH4, with >97% methanol conversion, could be produced in a 1 cm3 bed volume of our novel microfibrous entrapped ZnO-CaO/Al2O3 catalyst composite at 470 °C with a high weight hourly space velocity (WHSV) of 15 h−1 using steam/methanol (1.3/1) mixture as feedstock. Compared to a packed bed of 100–200 μm ZnO-CaO/Al2O3, our composite bed provided a doubling of the reactor throughput with a halving of catalyst usage.


Graphical abstract
Keywords
Hydrogen; Monolithic catalyst; Methanol steam reforming; ZnO; CaO; Fuel cells