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In relation to this article, we declare that there is no conflict of interest.
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Received May 31, 2021
Accepted November 9, 2021
articles This is an Open-Access article distributed under the terms of the Creative Commons Attribution Non-Commercial License (http://creativecommons.org/licenses/bync/3.0) which permits unrestricted non-commercial use, distribution, and reproduction in any medium, provided the original work is properly cited.
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Roasting and leaching process of iron sulfate to separate zinc and iron from blast furnace dust

1School of Metallurgical Engineering, Xi'an University of Architecture and Technology, Xi'an 710311, China 2Guangdong Jiana Energy Technology Co. Ltd, Qingyuan 513056, China 3Qingyuan Jiazhi New Materials Research Institute Co. Ltd., Qingyuan, 511517, China
Korean Journal of Chemical Engineering, May 2022, 39(5), 1339-1349(11), 10.1007/s11814-021-1012-0
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Abstract

The physical phase analysis and thermodynamic calculations of blast furnace dust were performed using Xray diffraction fluorescence spectrometer, X-ray diffractometer, scanning electron microscope, energy spectrometer, and Factsage software. The leaching pattern and mechanism of zinc elements were studied by a roasting-leaching method. The results showed that the conversion of zinc ferrite to zinc sulfate could be realized when the roasting temperature range was 500-730 ℃, which was convenient for zinc leaching. A better roasting condition could be obtained when theroasting temperature was 600 ℃, roasting time was 60 min, and molar ratio of ferric sulfate was 1.2 : 1. Under these conditions, the zinc and iron leaching rates were 84.57% and 24.51%, respectively, at a sulfuric acid concentration of 110 gL-1, liquid-solid ratio of 10 : 1 mLg-1, leaching time of 60min, stirring speed of 400 rpm, and leaching temperature of 80 ℃. The leaching process of zinc from blast furnace dust sulfate roasting products agreed with the unreacted core model, and internal diffusion was the restrictive step. The kinetic equation of the leaching process was 1-2R/3-(1-R)2/3=0.47t, the apparent activation energy of the leaching reaction was 17.4 kJmol-1, and the reaction order was 1.908.

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