Abstract Carbon Capture in Molten Salts (CCMS) is a high temperature method for extracting CO 2 from a variety of flue gases related to power generation and carbon-intensive industries. The chemical principles are similar to those in calcium looping in the solid state; a carbonation reaction of CaO with CO 2 to form CaCO 3 followed by regeneration of CO 2 through the reverse reaction. In CCMS, the active substances (CaO/CaCO 3 ) are dissolved or partly dissolved in molten salts, allowing fast reaction kinetics, high CO 2 sorption capacities, and avoiding solids attrition issues. In our previous studies, the focus has been on the total CO 2 sorption capacity and demonstration of cyclic absorption and desorption. Experiments have been performed with up to 20 wt% CaO in molten CaCl 2 and eutectic CaF 2 /CaCl 2 . It has been demonstrated that up to 85% of the CaO reacts during absorption, and ∼100% of the CaCO 3 is decomposed during desorption. No degradation of the sorbent has been observed after 12 cycles. In the present study, the focus is turned to the reaction kinetics between CO 2 and CaO. The raw data from previous experiments are analyzed to obtain the sorption capacity (g CO 2 / 100 g sorbent) as a function of time, and the linear region of the capacity is further used to evaluate the reaction kinetics. The effect of absorption temperature, molten salt composition, CaO content and cyclic CO 2 capture is studied. The results show that CaF 2 /CaCl 2 is more favorable for CCMS than pure CaCl 2 ; the kinetically controlled regime lasts longer and the total sorption capacity is higher. For both of the salt mixtures, the sorption capacities are stable during cyclic CO 2 capture, without any deterioration of the reaction kinetics.