This
paper presents a steady-state simulation of sorbent-enhanced
steam methane reforming in turbulent fluidized bed reactors. The effects
of different operating conditions are assessed, including the reactor
temperature, operating pressure, gas feed composition, and sorbent/methane
molar feed ratio. The potential system performance is also evaluated
when hydrogen perm-selective membranes are installed inside the reactor.
Increasing the sorbent/methane molar feed ratio and decreasing the
methane feed concentration can enhance the methane conversion, hydrogen
yield, and product purity. On the other hand, the reactor performance
depends strongly upon the system pressure, with higher temperatures
required for pressurized operation. In situ hydrogen
removal is shown to enhance the methane conversion and hydrogen production
yield, while reducing the hydrogen concentration in the reformer off-gas.
A predictive model is used to determine the operating conditions required
for steam and methane-concentrated oxy-fuel calciners. The methane-concentrated
oxy-fuel calciner is shown to benefit from a lower reactor temperature,
higher hydrogen production yield, and lower CO2 emissions.