Abstract

Effective recycling of zinc-containing industrial wastes, most importantly electric arc furnace dust, is of tremendous importance for the circular economy of the steel and zinc industry. Herein, we propose a comprehensive kinetic model of the combined carbothermic and metallothermic reduction of zinc oxide in a metal bath process. Pyro-metallurgical, large-scale lab experiments of a carbon-saturated iron melt as reduction agent for a molten zinc oxide slag were performed to determine reaction constants and accurately predict mass transfer coefficients of the proposed kinetic model. An experimentally determined kinetic model demonstrates that various reactions run simultaneously during the reduction of zinc oxide and iron oxide. For the investigated slag composition, the temperature-dependent contribution of the metallothermic zinc oxide reduction was between 25 and 50 pct of the overall reaction mechanism. The mass transfer coefficient of the zinc oxide reduction quadrupled from 1400 °C to 1500 °C. The zinc recovery rate was > 99.9 pct in all experiments.

Highlights

  • ZINC (Zn) is the fourth most produced metal worldwide (13 million tons per year) following iron, aluminum and copper

  • We present mass transfer coefficients for the ZnO and FeO reduction accounting for all experimental assumption to assist the development of industrial electric arc furnace dust (EAFD) recycling processes

  • In the following we present the construction of a mathematical model that describes in detail the characteristics of the reduction reactions between a carbon-saturated iron melt and a synthetic slag system containing ZnO

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Summary

Introduction

ZINC (Zn) is the fourth most produced metal worldwide (13 million tons per year) following iron, aluminum and copper. LEGERER is with the Rural Clinical School, Faculty of Medicine, University of New South Wales, Sydney, NSW 2052, Australia

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