CFD Modeling of Copper Smelting - Peru 2012

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    Computational Fluid Dynamic

    (CFD) modeling of copper flash

    smelting and converting

    Hong Yong Sohn

    Department of Metal lurgical Engineer ing

    University of Utah, Salt Lake City, Utah, U.S.A.

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    Outokumpu Flash Furnace

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    Process Design andMathematical Modeling

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    Process Modeling

    Earlierpyrometallurgical processes: Batch, equil.

    conditionsNewer processes: Higher productivity, higher

    intensity (Rate processesare inportant.)

    Need for transport property data, more reliable

    thermochemical data

    Improved tools have become available:

    Computers, analytical instruments, electronic

    apparatusesCFD: Flash smelting processes

    Thermochemistry of minor element behavior

    Gas injection into melts

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    x

    y

    z

    OXYGEN-ENRICHED AIR

    MOLTEN BATH

    SURFACE

    TO UPTAKE

    SHAFT

    O2

    SO2

    I

    REACTION SHAFT

    COPPER MATTE

    PARTICLES

    PARTICLE CLOUDS

    Computational Fluid Dynamics Modeling

    of Flash Smelting and Converting Furnaces

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    Components of Computer Modeling

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    Turbulent Flow Phenomena

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    Gas-Phase Equations

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    Particle-Phase Equations

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    Apparatus for Particle-Dispersion Analysis

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    Digitized Image of Particles in Gas Jet

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    Experimental vs. Computed Particle Distribution

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    Schematics of Pilot Flash Furnace Facility

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    Results for Flash Smelting Experiment

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    6-Jet Entry Pilot Burner

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    Gas Velocity Vectors in Laboratory Furnace(6-Jet Entry System)

    The largest vector

    represents 1.32 m/s.

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    (a) single axial entry burner (b)85-distributor cone burner

    (Numbers indicate velocity in m/s)

    Gas velocity fields in an industrial

    flash converting furnace

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    (a) single axial entry burner (b)85-distributor cone burnerNumbers indicate logarithm of number of particles per cubic meter

    Particle number density in an industrial

    flash converting furnace

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    (a) single axial entry burner (b) 85-distributor cone burner

    Gas temperature in an industrial

    flash converting furnace

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    (a)single axial entry burner (b)85-distributor cone burner

    Oxygen concentration in an industrial

    flash converting furnace

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    Results for Flash Converting Experiment

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    Results for Flash Converting Experiment

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    Results for Flash Converting Experimen

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    Nippon Mining and Metals Co. (Nikko)

    Modified operating conditions to double their

    feed rate (production rate) without changing

    their furnace based on modeling results.

    [Y. Yasuda did graduate work on CFD of flash furnaces at Utah.]

    Suzuki, Y., Suenaga, C., Ogasawara, M., and Yasuda, Y., 1998, Productivity increase in flash smelting furnace operation atSaganoseki Smelter & Refinery, in Sulfide Smelting 98, Current and Future Practices, J.A. Asteljoki and R.L. Stephens, eds., TMS,Warrendale, PA, pp. 587-595.

    Y. B. Hahn and H. Y. Sohn, Mathematical Modeling of Sulfide Flash Smelting Process: Part I. Model Development and Verificationwith Laboratory and PilotPlant Measurements for Chalcopyrite Concentrate Smelting, Metall. Trans. B, 21B, 945958 (1990).

    An Example of Application

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    Ready availability of CFD capabilityPowerful yet inexpensive computers

    Commercial softwareNeed to learn how to use it

    Like driving a car

    Benefits:Optimal designImproved control and operationCan perform many test runs at low costs

    Concluding Remarks

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    End of Presentation