Catalysts | |
Ir-Based Bimetallic Catalysts for Hydrogen Production through Glycerol Aqueous-Phase Reforming | |
Miguel Ruiz-Gómez1  Francisco Espinosa-Moreno2  JuanC. Chavarria-Hernandez2  Saúl Tlecuitl-Beristain3  Putrakumar Balla4  Wenjie Shen4  | |
[1] CONACYT-Departamento de Física Aplicada, CONACYT-CINVESTAV-IPN, 97310 Mérida, Yucatán, Mexico;Centro de Investigación Científica de Yucatán, Parque Científico y Tecnológico de Yucatán, Carretera Sierra Papacal–Chuburna Puerto, km 5. Sierra Papacal, 97302 Mérida, Yucatán, Mexico;Ingeniería en Biotecnología, Universidad Politécnica de Tlaxcala, San Pedro Xalcatzinco, 90180 Tepeyanco, Tlaxcala, Mexico;State Key Laboratory of Catalysis, Dalian Institute of Chemical Physics, Chinese Academy of Sciences, 457-Zhong Shan Road, Dalian 116023, China; | |
关键词: iridium; glycerol; aqueous-phase reforming; hydrogen production; | |
DOI : 10.3390/catal8120613 | |
来源: DOAJ |
【 摘 要 】
Iridium, Iridium-Nickel and Iridium-Copper catalysts were prepared by incipient wetness impregnation and evaluated in the aqueous-phase reforming of glycerol using La2O3 or CeO2 as supports. The catalysts were characterized by N2 physisorption, XRD, H2-TPR, XPS, and EDS. The reactions were carried out in a fixed bed reactor feeding a solution of glycerol (10 wt %) in water, at 270 °C and 58 bar. All IrNi catalysts showed higher activity than Ir and IrCu, and in general, La2O3 catalysts showed a better performance when compared to CeO2 catalysts. The highest hydrogen production yield was reached by bimetallic IrNi catalysts with over 250 µmol min−1 gcat−1 for La2O3 and 150 µmol min−1 gcat−1 for CeO2.
【 授权许可】
Unknown