In order to understand and control the formation of dioxins and furans (PCDD/Fs) in iron ore sinter plants, a CFD model of iron ore sintering, combined with the kinetic models of 14 relevant chemical reactions and thermodynamic calculations of dioxin formation, has been developed to simulate the concentrations of the gaseous species, temperatures of the gas and solid, velocity of the gas, temperature zones, and residence time of the gas in each temperature zone. The predicted off-gas compositions, the velocities of the gas, and the trends for the gas temperature at the bottom of the bed have been compared with measured data from a sinter plant, and good agreement has been obtained. From the predicted temperature zones of the gas and solid, the predicted residence time of the gas in each zone, and thermodynamic conditions of PCDD/F formation, the PCDD/F formation in sinter plants has been discussed. The dioxins are formed in the critical temperature region of 250°C to 450°C below the combustion zone in the bed, are then carried downward with the gas, and are condensed close to the bottom of the sinter bed. Transported to the discharge end with the solid mixture, they are again released into the gas phase when the flame front approaches the bottom. The dioxins are also formed in the last wind boxes when the hot off-gases cool and reach the critical temperature range. These pathways on PCDD/F formation can explain the industrial observations well. The preceding information may assist in the effective control or elimination of dioxin formation in iron ore sinter plants.