To reach the carbon peak by 2030
and achieve carbon neutrality
by 2060, the implementation of low-carbon combustion approaches for
fossil fuels (especially coal, a high-carbon fuel) is urgent in China.
Chemical looping combustion (CLC) has been considered as one of the
most promising technologies for low-carbon, efficient, and clean utilization
of coal. However, a low-cost and high-performance oxygen carrier (OC)
holds the bottleneck that constrains the industrial application of
coal-fueled CLC. In this paper, a low-cost composite OC named Cu13.0Red87.0@C
(with the mixing mass ratio of copper ore to red mud being 13.0:87.0,
except for a 20 wt % cement bonder) was first prepared by the hydroforming
method and then systematically evaluated by designing CLC tests in
a semi-continuous fluidized bed using lignite as fuel. The results
showed that this composite OC exhibited superior combustion performance
in comparison to pure red mud. Moreover, it was found that increasing
the temperature could significantly improve the average carbon capture
efficiency but had a relatively small positive effect on the average
CO2 yield. Additionally, with the elevation of the oxygen/fuel
ratio, the resulting average carbon capture efficiency and average
CO2 yield both tended to increase. Generally, the semi-continuous
unit can simulate the continuously operated fuel reactor with an adjustable
bed inventory and solid circulation rate, and it is easy to attain
smooth operation of ca. 30 min, achieving both carbon capture efficiency
and a CO2 yield of ca. 90%.