This work presents a simulation study of several Ca—Cu looping variants with CO
2
capture
aiming at both parameter optimization and exergy analysis of these Ca—Cu looping systems. Three kinds of Ca—Cu looping are considered: 1) carbonation-calcination/reduction-oxidation; 2) carbonation-oxidation-calcination/reduction and 3) carbonation/oxidation-calcination/reduction. A conventional Ca looping is also simulated for comparison. The influences of the calcination temperature on the mole fractions of CO
2
and CaO at the calciner outlet
the CaCO
3
flow rate on the carbonator performance and the Cu/Ca ratio on the calciner performance are analyzed. The second kind of Ca—Cu looping has the highest carbonation conversion. At 1 × 10
5
Pa and 820 °C
complete decomposition of CaCO
3
can be achieved in three Ca—Cu looping systems
while the operation condition of 1 × 10
5
Pa
840 °C is required for the conventional Ca looping system. Furthermore
the Cu/Ca molar ratio of 5.13-5.19 is required for the Ca—Cu looping. Exergy analyses show that the maximum exergy destruction occurs in the calciner for the four mod
es and the second Ca—Cu looping system (i.e.
carbonation-oxidation-calcination/reduction) performs the highest exergy efficiency
up to 65.04%
which is about 30% higher than that of the conventional Ca looping.
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