A catalytic fixed-bed recycle reactor was proposed to increase the level of reaction conversion in conducting the hydrogenation of CO2. The hydrogenation of CO2 was carried out over Fe-K/Al2O3 catalyst. The conversion of carbon dioxide (XCO2) increased with increasing reaction temperature and modified residence time (τmod) in the fixed bed single reactor. In series reactors, the XCO2 increased up to the level of 68.5% (T=300 ℃, P=1.0 MPa, H2/CO2=3 and SV=1,000 ml/gcat.hr) in comparison with the level of 40.8% in the fixed bed single reactor at the same conditions. The XCO2 increased with increasing recycle ratio(R) and exhibited a maximum value with increasing total space velocity (SVT). The maximum XCO2 was the level of 75.6% (T=300 ℃, P=1.0 MPa, H2/CO2=3, R=6 and SVT=4,000 ml/gcat.hr) in the recycle reactor when the SVT was 5,000 ml/gcat.hr. From the results of this study, it was found that the recycle ratio of reactant gas, effective separation of water vapor and liquid hydrocarbon, modified residence time and equilibrium conversion level of the reaction were important factors to determine the conversion level of the hydrogenation of carbon dioxide.