Abstract
Natural gas was reformed with anode off-gas of a solid
oxide fuel cell (SOFC) in a laboratory reactor using
model gases. Nickel and precious metal catalysts were
tested at 650 °C and 700 °C inlet temperature. The oxygen
to carbon (O/C) molar ratio of the inlet gas was varied
between 0.3 and 2.0 to find out the limit O/C ratio for
carbon formation. Two natural gas compositions were used:
low purity Danish gas and high purity Russian gas. The
experimental limit was found to be 0.9-1.25 for nickel
catalyst and 0.5-0.75 for precious metal catalyst. The
limit was higher with Danish gas than with Russian gas in
the experiments with nickel catalyst but this effect was
not observed with the precious metal catalyst. A good
correlation between experimental results and
thermodynamic calculations was found using the principle
of actual gas: the calculations estimated the O/C limit
ratio for nickel at 1.0 and for precious metal catalyst
between 0.5 and 0.7.
Original language | English |
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Pages (from-to) | 1548-1558 |
Journal | International Journal of Hydrogen Energy |
Volume | 40 |
Issue number | 3 |
DOIs | |
Publication status | Published - 2015 |
MoE publication type | A1 Journal article-refereed |
Keywords
- anode off-gas recycling
- reforming
- precious metal catalyst
- nickel catalyst
- carbon formation
- solid oxide fuel cell