Steam reforming of biomass tar producing H2-rich gases over Ni/MgOx/CaO1-x catalyst.
Series nickel catalysts Ni/MgO(x)/CaO(1-)(x) (x=0.3, 0.5, 0.7, Ni: 5 wt%) were prepared and tested in fixed-bed reactor for biomass tar steam reforming, toluene as tar destruction model compound. Different ratios of MgO and CaO were mixed to simulate dolomite as Ni support. Two preparation methods: solid mixing with (SMW) and without water (SM) were used, the preparation methods and concentration of MgO had an important influence on toluene conversion and products. Catalysts prepared by SM method exhibited higher performance on toluene conversion, resulted in higher H(2) yield, and also, higher CO(2) and lower CO selectivity with higher temperature. For the same preparation method, higher concentration of MgO resulted in higher toluene conversion, and also influence on CO, CO(2) selectivity, but no obvious influence on the H(2) yield. Catalysts were characterized by BET, X-ray diffraction (XRD), SEM.
Li
Chunshan
C
EcoTopia Science Institute, Nagoya University, Furo-cho, Chikusa-ku, Nagoya, Aichi, Japan. li_chunshan@nagoya-u.jp
Hirabayashi
Daisuke
D
Suzuki
Kenzi
K
D018533:Biomass; D017610:Calcium Compounds / Q000737:chemistry*; D002384:Catalysis; D005740:Gases / Q000737:chemistry*; D006859:Hydrogen / Q000737:chemistry; D008277:Magnesium Oxide / Q000737:chemistry*; D008855:Microscopy, Electron, Scanning; D009532:Nickel / Q000737:chemistry*; D010087:Oxides / Q000737:chemistry*; D013227:Steam; D013638:Tars / Q000737:chemistry*; D014961:X-Ray Diffraction
D017610:Calcium Compounds; D005740:Gases; D010087:Oxides; D013227:Steam; D013638:Tars; D008277:Magnesium Oxide; D009532:Nickel; D006859:Hydrogen; C016538:lime