The partial substitution of O 2 with CO 2 in steelmaking process is an important technology to reduce CO 2 emission and recycle. In order to improve CO 2 -O 2 decarburization utilization, the decarburization kinetics of Fe-C melt with CO 2 -O 2 mixed gas have been studied using 13 CO 2 -18 O 2 dual isotope tracing method and established the decarburization kinetic model. The results show that less than 40% of the oxygen is partially replaced by CO 2 , which improves the O 2 utilization involved in the decarburization reaction and the CO 2 utilization is still more than 80%. For the rate limiting steps, regarding O 2 , it is governed by the mixed control mechanism involving gas-phase mass transfer and interfacial chemical reaction; regarding CO 2 , with the increase of CO 2 partial pressure, the rate limiting step changes from the mixed control to gas-phase mass transfer control only. As bath temperature increase from 1723 to 1873 K, the overall decarburization rate increases; bath temperature mainly affects O 2 decarburization rates, whereas, the rates of CO 2 are not significantly affected. The apparent activation energy of CO 2 -O 2 mixed gas decarburization is 21.5 kJ•mol -1 .