The evaluation of chemical looping combustion (CLC) for CO2 capture was conducted via a thermogravimetric analyzer (TGA) and a laboratory-scale fluidized bed using pine sawdust (PS) as fuel and metal ferrites, MFe2O4 (M = Cu, Ni and Co), as oxygen carriers. Metal ferrites were prepared by sol-gel method. The fresh, reduced and after five redox cycles oxygen carriers were characterized by X-ray diffraction (XRD), scanning electron microscopy (SEM) and accelerated surface area porosimetry. Thermodynamic simulation was performed using software HSC Chemistry 6.0. The TGA results indicated that CuFe2O4 shows a lower initial reaction temperature, and CoFe2O4 has a faster oxygen uptake rate. Both carbon conversion (xc) and carbon capture efficiency (eta(co2)) increased with temperature. The maximum values of xc and n CO2 were 96.86% and 95.48%, 95.45% and 94.25%, and 95.17% and 94.04% for CuFe2O4, CoFe2O4, and NiFe2O4 at 900 degrees C, respectively. The CuFe2O4 shows higher reaction reactivity, while NiFe2O4 has a higher catalytic activity for decomposition of tar in fluidized bed tests. The XRD results show CoFe2O4 is more readily reduced to FeO, which agreed with the results of thermodynamic simulation, and three metal ferrites can be regenerated completely after five cycles. The values of x(c) and eta(co2) remained high for both CuFe2O4 and CoFe2O4, while a significant decrease in x(c) and eta(co2) for NiFe2O4 was observed after five cycles due to significant sintering. Both CuFe2O4 and CoFe2O4 are more applicable as oxygen carriers in biomass CLC compared with NiFe2O4. (C) 2016 Elsevier B.V. All rights reserved.