Under the operating parameters of
a chemically recuperated gas
turbine (CRGT), the low-temperature methane steam reforming test bench
is designed and built; systematic experimental studies about fuel
steam reforming are conducted. Four different reforming forms are
employed, including catalyst-only reforming, plasma-only reforming,
piecewise synergistic reforming, and parallel synergistic reforming.
A better reforming form for CRGT was determined by analyzing the effect
of methane space velocity, steam-to-carbon ratio of fuel reforming
(S/C), wall temperature, and plasma input power. All of the above
factors had an effect on the reforming performance, but a direct and
significant effect separately on effective carbon recovery rate, total
enthalpy increasing rate, methane conversion, and fuel heating value
increasing rate. The effective carbon recovery rate was taken as the
chief indicator for choosing the right operating conditions, determining
a best methane space velocity of 680 mL/(gcat·h).
With the increase of S/C, total enthalpy increasing rate had a significant
improvement; wall temperature had a positive effect on reforming,
especially in synergistic catalysis. The effect of input power was
linked with wall temperature in parallel synergistic reforming, with
a greater effect at a higher temperature. Combining the experimental
results with the theory analysis, parallel synergistic reforming is
best, with a methane conversion of 51.23% and total enthalpy increasing
rate of 25.73% at a wall temperature of 500 °C, an input power
of 84.53 W, and an S/C value of 2.