A kinetic model was prepared for the simulation of the production of H
CN in a yttria-stabilized-zirconia cell that uses CH4-NH3 mixtures as
fuel. The model considers 14 surface reactions occuring simultaneously
at the anode. The effects of temperature, O2-flux, inlet gas composit
ion, and inlet gas velocity on the HCN yield and on the overall exothe
rmicity of the system were examined. It was found that the cell can op
erate without external heat supply if the CH4/NH3 feed ratio is higher
than 1.25. Two different cell designs were examined, one in which the
anode is inside the zirconia tube, and one in which air flows inside
the tube and the fuel flows outside perpendicular to the direction of
air flow. The latter design exhibits certain additional advantages ove
r the traditional tubular cell design.