Enhanced hydrogen production over Ni-M alloys (M = Co, Zn) formed from hydrotalcite-derived structures for aqueous-phase reforming of xylose

被引:0
|
作者
Khosashi, Owen [1 ,2 ]
Kim, Yoondo [1 ,3 ]
Cho, Seoyeon [1 ,4 ]
Jeong, Hyangsoo [1 ,2 ]
Kim, Yongmin [1 ]
Yoon, Sung Pil [1 ]
Song, Kwang Ho [3 ]
Nam, Suk Woo [1 ]
Choi, Sun Hee [1 ,2 ]
Sohn, Hyuntae [1 ,2 ]
机构
[1] Korea Inst Sci & Technol KIST, Ctr Hydrogen & Fuel Cell Res, Clean Technol Res Div, Seoul 02792, South Korea
[2] Univ Sci & Technol UST, KIST Sch, Dept Energy & Environm Engn, Seoul 02792, South Korea
[3] Korea Univ, Dept Chem & Biol Engn, Seoul 02841, South Korea
[4] Seoul Natl Univ Sci & Technol, Dept Fine Chem, Seoul 01811, South Korea
基金
新加坡国家研究基金会;
关键词
Hydrogen; Aqueous phase reforming; Xylose; Nickel; Promoter; Hydrotalcite; ETHYLENE-GLYCOL; RENEWABLE HYDROGEN; CATALYTIC-ACTIVITY; METHANE; TEMPERATURE; PERFORMANCE; GLYCEROL; ETHANOL; BIOMASS; HYDROCARBONS;
D O I
10.1016/j.apsusc.2024.162229
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Non-noble metal-based catalysts derived from Ni-hydrotalcite, incorporating various metal promoters (Cu, Co, Ca, Mg, and Zn) were studied for Aqueous-phase reforming (APR) of xylose. The formation of a hydrotalcite structure in the as-prepared samples and their transition into mixed-metal oxides upon calcination was confirmed. During subsequent reduction, more reducible promoters (Cu, Co, and Zn) formed alloys with Ni, while less reducible promoters (Ca and Mg) remained in their oxide form within the catalyst. NiZnAl and NiCoAl catalysts outperformed NiAl, achieving higher hydrogen yields and production rates per gram of Ni for APR of xylose. NiZnAl exhibited the highest catalytic activity, owing to the formation of a NiZn alloy with increased electron density, leading to a lower surface acidity and enhanced adsorbate-metal interactions, thereby improving the reforming activity. The proposed Ni-hydrotalcite-derived catalyst offers a simple and cost-effective solution for scalable xylose reforming with high catalytic performance and stability.
引用
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页数:15
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