Chapter 32

Heat Losses to Furnace Coolers as a Function of Process Intensity

M.W. Kennedy

M.W. Kennedy

Department of Materials Science and Engineering, Norwegian University of Science and Technology, Trondheim, Norway

ProVal Partners, SA, Avenue de Sévelin 6 b, Lausanne, Switzerland

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A. MacRae

A. MacRae

MacRae Technologies, Inc., 1000 Silver Maple Lane, Hayward, CA, USA

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H. Haaland

H. Haaland

4Elkem Technology, Drammensveien 169-171, Oslo, Norway

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First published: 03 February 2016

Summary

Furnace refractories are in most cases chemically incompatible with smelter slag, which leads to a steady erosion in their thickness over time. Once too thin, refractory walls become mechanically unstable and catastrophic failure can result. Historically, external shell cooling was applied to generate a freeze lining of slag and thus prevent refractory erosion. Many modern high intensity smelting furnaces instead maintain their physical integrity by the use of internally cooled wall panels, plates or finger coolers. An initial refractory lining is often installed inside of the coolers, such that the furnace originally operates with a temperature (insulated) rather than a heat flux (freeze lined) boundary condition. This paper examines the change in slag-wall heat transfer coefficient and slag superheat as a function of process intensity. The implications of the changes in heat transfer on residual brick thickness are explored using analytical modelling.

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