Chemical looping combustion (CLC)
technology has emerged as one
of the most important clean fossil fuel combustion technologies, because
it allows for sequestration of CO2 with a minimal increase
in energy requirements and fuel demand in comparison to traditional
plants. In the framework of the Chinese–European Emission-Reducing
Solutions project, the core technology of the CLC process is being
developed in a 3 MWth system prototype for demonstration
in an operational environment using petcoke as fuel. One of the main
objectives is the selection of the oxygen carrier because it will
impact the design and sizing of the demonstration unit as well as
the nominal power of the unit. Two minerals, ilmenite T1 and LY Mn
ore, with high potential for a well-performing oxygen carrier were
tested in a 10 kWth continuous pilot unit. The collected
fines were analyzed by scanning electron microscopy and X-ray fluorescence
analysis to characterize the compositional and morphological evolution
of the particles during operation. The performance of both oxygen
carriers was compared with respect to solid fuel conversion, capacity
for oxygen transfer, and particle lifetime in continuous circulation.
A higher methane conversion can be obtained using ilmenite, while
LY Mn is better at converting petcoke. Where the reduction potential
of oxygen carriers is concerned, it was observed that LY Mn ore has
a high initial R
0ΔX value (R
0ΔX =
0.8), which leads to a shorter activation period in comparison to
ilmenite T1, which requires a longer activation period to reach its
full potential. LY Mn ore is however more sensitive to attrition than
ilmenite, under similar operating conditions, which is a critical
characteristic for large-scale deployment. Finally, key operating
parameters were identified for large-scale unit operation, including
fuel reactor temperature, oxygen carrier flow rate, and fuel flow
rate.