Chemical looping combustion (CLC) offers inherent CO2 capture and cascade energy utilization.
Key challenges include cost-performance balance of oxygen carriers and reactor optimization.
Commercialization is hindered by operational complexities and efficiency gaps.
Advancing CLC requires cost-effective oxygen carriers and standardized reactor designs.
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The graphical summary of this review's framework.
Development status of chemical looping combustion
A brief description of energy cascade utilization
The pollutants in-situ control performance of CLC
Schematic description of the liquid fuel injector
Energy penalty for a
Development of the CLC units.
(A) Correlation between the performance and cost of typical OCs;159 (B) Gaseous species yields and combustion efficiency among 20 cycles at 950 °C;177 (C) Comparison of the heterogeneous reduction kinetics between CMTF_Ind and CMTF_Lab;182 (D) TG curves of CMTF and CM0.625TF-Mg OC;184 (E) Workflow of developing a ML model for OCs in the CL process.185
(A) Relative magnitudes of reaction rates of various reactions in CLC/CLOU of coal;159 (B) The DTA curves and heat release capacity of Copper-iron ore OCs;174 (C) 5 kWth CLC reactor at SU;189 (D) 30 kWth CLC reactor at Tsinghua University;190 (E) Schematic diagram of CS and a picture of the 50 kWth iG-CLC reactor.156