TY - JOUR
T1 - Ecofriendly extraction of zinc from hazardous electric arc furnace dust via sulphating roasting
T2 - Non-isothermal and isothermal kinetics analyses
AU - Chen, Yangfan
AU - Li, Jiangling
AU - Teng, Wenxin
AU - Song, Jiangfeng
AU - Liu, Weizao
AU - Ren, Shan
AU - Yang, Jian
AU - Liu, Qingcai
N1 - Publisher Copyright:
© 2023 The Institution of Chemical Engineers
PY - 2023/11
Y1 - 2023/11
N2 - Electric arc furnace dust (EAFD) formed during steelmaking in electric arc furnace is a hazardous solid waste that is rich in zinc and iron. In our previous study, we realized the efficient extraction and separation of Zn and Fe from EAFD by co-roasting with FeSO4·7H2O followed by water leaching processes, which achieved a high extraction rate of Zn (98.79 %) and a low extraction rate of Fe (0.11 %). However, the high temperature would lead to high energy consumption. Therefore, non-isothermal kinetic and isothermal kinetic were exploited in this study to analyze the heating and holding process for further optimizing roasting conditions. The heating process was divided into four reaction stages with different reaction models. Moreover, the holding process was also divided into two reaction stages with the Anti-Jander 3D diffusion model and Z-L-T 3D diffusion model, respectively. The major reactions in the heating and holding process were defined by thermodynamic equilibrium calculations and in situ X-ray diffraction. The rate-determining step was deduced as the desulfurization of Fe2(SO4)3 with a three-dimensional diffusion reaction model. Aiming to accelerate Fe2(SO4)3 desulfurization, the insulation conditions of this process were optimized from 675 °C for 3 h to 600 °C for 3 h, significantly reducing energy consumption.
AB - Electric arc furnace dust (EAFD) formed during steelmaking in electric arc furnace is a hazardous solid waste that is rich in zinc and iron. In our previous study, we realized the efficient extraction and separation of Zn and Fe from EAFD by co-roasting with FeSO4·7H2O followed by water leaching processes, which achieved a high extraction rate of Zn (98.79 %) and a low extraction rate of Fe (0.11 %). However, the high temperature would lead to high energy consumption. Therefore, non-isothermal kinetic and isothermal kinetic were exploited in this study to analyze the heating and holding process for further optimizing roasting conditions. The heating process was divided into four reaction stages with different reaction models. Moreover, the holding process was also divided into two reaction stages with the Anti-Jander 3D diffusion model and Z-L-T 3D diffusion model, respectively. The major reactions in the heating and holding process were defined by thermodynamic equilibrium calculations and in situ X-ray diffraction. The rate-determining step was deduced as the desulfurization of Fe2(SO4)3 with a three-dimensional diffusion reaction model. Aiming to accelerate Fe2(SO4)3 desulfurization, the insulation conditions of this process were optimized from 675 °C for 3 h to 600 °C for 3 h, significantly reducing energy consumption.
KW - EAFD
KW - FeSO·7HO
KW - Isothermal kinetic
KW - Non-isothermal kinetic
KW - Zn extraction
UR - https://www.scopus.com/pages/publications/85172684429
U2 - 10.1016/j.psep.2023.09.063
DO - 10.1016/j.psep.2023.09.063
M3 - 文章
AN - SCOPUS:85172684429
SN - 0957-5820
VL - 179
SP - 873
EP - 886
JO - Process Safety and Environmental Protection
JF - Process Safety and Environmental Protection
ER -