Aiming at the problems of large tar influence and low
gasification
efficiency in traditional biomass gasification, in this paper, a chemical
looping reforming (CLR) of volatiles from biomass pyrolysis based
on decoupling strategy is proposed to convert macromolecular volatiles
into hydrogen-rich syngas. A series of highly active and selective
oxygen carrier (OC) SBA-15 encapsulating LaFe
x
M1–x
O3 (M = Ni,
Cu, Co) for the biomass CLR process was developed. Reaction kinetics
and cycling performance of toluene CLR process on LaFe0.6Co0.4O3@SBA-15 OCs were explored. Experimental
results showed that the encapsulation effect gave the metal oxide
a better dispersion, reduced the sintering, and improved the reaction
performance. Compared with LaFeO3, the toluene conversion
increased from 52.3% to 79.7%, the CO selectivity improved from 57.0%
to 87.4%, and the oxygen release (OR) increased by 100% after encapsulation
in SBA-15. Due to the substitution of Ni2+, Cu2+ and Co2+ on Fe3+, more oxygen vacancies in
OCs were created, and both conversions of toluene and selectivity
of CO were improved. Among them, the incorporation of Co had the best
performance, the toluene conversion was 81.6%, and the CO selectivity
was 96.8%. The kinetics of the LaFe0.6Co0.4O3@SBA-15 reaction was solved using a gas–solid reaction
model with an activation energy of 103.9 kJ mol–1 and a pre-exponential factor of 123.8 s–1. The
performance of LaFe0.6Co0.4O3@SBA-15
was tested for 10 cycles, and it was found that conversion of toluene
and CO selectivity were well-maintained at 90.0%–92.0% and
93.0%–96.0%, respectively. This study could guide the selection
of OCs in reforming macromolecular volatiles from biomass pyrolysis
to produce hydrogen-rich syngas.