TY - JOUR
T1 - Production of CO-free hydrogen through the decomposition of LPG and kerosene over Ni-based catalysts
AU - Takenaka, Sakae
AU - Kawashima, Kenji
AU - Matsune, Hideki
AU - Kishida, Masahiro
N1 - Funding Information:
This study was supported by a program for “developments for the utilization of new fuels” in Japan Petroleum Energy Center.
PY - 2007/4/11
Y1 - 2007/4/11
N2 - The catalytic performance of Ni-based catalysts for the decomposition of hydrocarbons of C3-C8 into CO-free hydrogen and carbon fibers was investigated in order to produce CO-free hydrogen as a fuel for PEFC from liquefied petroleum gas (LPG) and kerosene. The addition of Cu or Pd into Ni/SiO2 catalyst elongated its catalytic life for the propane decomposition. Especially, Ni-Pd/SiO2 catalyst showed higher activity and longer life for the decomposition of propane at 823 and 873 K, compared to Ni/SiO2 and Ni-Cu/SiO2 catalysts. Ni-Pd/SiO2 catalyst was deactivated gradually with time on stream during the decomposition of propane due to the deposition of large amounts of carbon. However, the activity of the catalyst for the propane decomposition was recovered completely by the gasification of deposited carbon with CO2 into CO. This result suggested that CO-free hydrogen and CO could be produced successively through the decomposition of hydrocarbons and the subsequent gasification of deposited carbon with CO2. Ni-Pd/SiO2 showed high catalytic activity for the decomposition of hydrocarbons of C6-C8 to form CO-free hydrogen. Thus, CO-free hydrogen was produced through the decomposition of commercial kerosene over Ni-Pd/SiO2 catalyst.
AB - The catalytic performance of Ni-based catalysts for the decomposition of hydrocarbons of C3-C8 into CO-free hydrogen and carbon fibers was investigated in order to produce CO-free hydrogen as a fuel for PEFC from liquefied petroleum gas (LPG) and kerosene. The addition of Cu or Pd into Ni/SiO2 catalyst elongated its catalytic life for the propane decomposition. Especially, Ni-Pd/SiO2 catalyst showed higher activity and longer life for the decomposition of propane at 823 and 873 K, compared to Ni/SiO2 and Ni-Cu/SiO2 catalysts. Ni-Pd/SiO2 catalyst was deactivated gradually with time on stream during the decomposition of propane due to the deposition of large amounts of carbon. However, the activity of the catalyst for the propane decomposition was recovered completely by the gasification of deposited carbon with CO2 into CO. This result suggested that CO-free hydrogen and CO could be produced successively through the decomposition of hydrocarbons and the subsequent gasification of deposited carbon with CO2. Ni-Pd/SiO2 showed high catalytic activity for the decomposition of hydrocarbons of C6-C8 to form CO-free hydrogen. Thus, CO-free hydrogen was produced through the decomposition of commercial kerosene over Ni-Pd/SiO2 catalyst.
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U2 - 10.1016/j.apcata.2007.01.042
DO - 10.1016/j.apcata.2007.01.042
M3 - Article
AN - SCOPUS:33947315445
SN - 0926-860X
VL - 321
SP - 165
EP - 174
JO - Applied Catalysis A: General
JF - Applied Catalysis A: General
IS - 2
ER -