Ni–Fe/Mg(Al)O alloy catalyst for carbon dioxide reforming of methane: Influence of reduction temperature and Ni–Fe alloying on coking. (27th November 2020)

• Record Type: Journal Article
• Authors: Wan, Chunsheng; Song, Kai; Pan, Jinhua; Huang, Min; Luo, Ruizhi; Li, Dalin; Jiang, Lilong
• Is Part Of: International journal of hydrogen energy. Volume 45:Number 58(2020)
• Page Start: 33574
• Page End: 33585
• Publication Date: 2020-11-27
• Subjects: Dry reforming of methane -- Nickel-iron alloy -- Hydrotalcite-like compounds; Hydrogen as fuel -- Periodicals; Hydrogène (Combustible) -- Périodiques; Hydrogen as fuel; Periodicals; 665.81
• DOI: 10.1016/j.ijhydene.2020.09.129
• Languages: English
• ISSNs: 0360-3199

Abstract

Abstract: Various Ni–Fe/Mg(Al)O alloy catalysts were obtained by calcination of Ni–Fe–Mg–Al hydrotalcite-like compounds, followed by reduction at different temperatures (973–1173 K). The characterizations of XRD and STEM-EDX suggest that the resulting Ni–Fe alloy particles are composition-uniform and size-controllable. The alloy composition is little affected by the reduction temperature, whereas the particle size (5.8–8.2 nm) increases with the increase of reduction temperature. This property is ascribed to the homogeneous distribution of nickel and iron species during the catalyst preparation. All of the Ni–Fe/Mg(Al)O alloy catalysts show relatively high and stable activity for CH4 –CO2 reforming during 25 h of investigation at 773–1073 K. Particularly, the 973 K-reduced catalyst exhibits higher coke-resistance due to its smaller particle size. E a -CH4 and CH4 -TPSR measurements indicate that Ni–Fe alloying inhibits CH4 dissociation. It is considered that during DRM CH4 is dissociated at the Ni sites and CO2 may be activated at the metal-support interface as well as the Fe sites. Ni–Fe alloying may inhibit CH4 dissociation and/or promote CO2 activation, thus contributing to the suppression of coke deposition. Highlights: Ni–Fe alloy particles are composition-uniform and size-controllable. Ni–Fe/Mg(Al)O catalysts shows good performance for DRM at 773–1073 K. The 973 K-reduced catalyst shows higher coke resistance due to small particle size. Ni–Fe alloying inhibits CH4 dissociation contributing to coke suppression.