| As a harmful substance in zinc metallurgy,ZnFe2O4 needs to destroy its crystal structure in order to recover zinc and iron.Most of the main treatment methods for ZnFe2O4 in the industry have the disadvantages of high energy consumption,large pollution,complicated process flow,and difficult residue treatment.In order to obtain zinc and iron elements directly,ZnFe2O4 is subjected to zinc-iron separation by molten salt electro-deoxidation,and the electrochemical reduction mechanism of ZnFe2O4 is studied.The thermodynamic analysis shows that the electrolytic reduction process of ZnFe2O4 is: ZnFe2O4 →FeO + ZnO →Fe + ZnO →Fe + Zn.And ZnFe2O4 is physically dissolved in NaCl-CaCl2 melts.The study of electrochemical reduction of ZnFe2O4 by electrochemical methods shows that the reduction process is a three-step process: The reduction ofFe3+ and Zn2+ is a quasi-reversible electrochemical reduction process controlled by diffusion on the Pt electrode,and a reversible and irreversible electrochemical reduction process controlled by diffusion on the Mo electrode.By studying the influence of electrolytic voltage,electrolytic temperature,electrolytic time and the influence of the intermediate product Ca2Fe2O5 in the electro-deoxidation process,it is shown that under the condition of 800℃ electrolysis for 8h,with the gradual increase of voltage,the step-reduction process of ZnFe2O4 is: ZnFe2O4 →FeO + ZnO →Fe + ZnO →Fe + Zn.The intermediate Ca2Fe2O5 is produced in the process of deoxidization,which has certain influence on fractional reduction and current change of ZnFe2O4 electro-deoxidation process.At the temperature of 800°C and a voltage of 1.8 V,full separation of zinc and iron can be achieved in melts for 8 hours of electrolysis. |