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Pressure drop in slurry pipe with stationary deposit

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    0095354 - ÚH 2011 RIV US eng C - Conference Paper (international conference)
    Matoušek, Václav
    Pressure drop in slurry pipe with stationary deposit.
    Proceedings of FEDSM2007. San Diego: ASME, 2007, Article no. 37322. ISBN 9780791842881.
    [Joint ASME/JSME Fluids Engineering Summer Conference /5./. San Diego, California (US), 30.07.2007-02.08.2007]
    R&D Projects: GA ČR GA103/06/0428
    Grant - others:GA MŠk(CZ) 1M0579
    Institutional research plan: CEZ:AV0Z20600510
    Keywords : bed friction * sheet flow * particle dispersion
    Subject RIV: BK - Fluid Dynamics

    The pressure-drop model is based on a description of prevailing mechanisms that are identified to govern solids dispersion and solids friction in slurry flows at different conditions (e.g. different average concentrations of solids above the stationary bed, different dimensions of the discharge area above the bed etc.). The proposed model is composed of continuity, momentum, boundary-friction and particle-dispersion equations. The empirical stratification-ratio equation relates the effect of particle dispersion within the slurry flow with the flow friction at the top of the stationary deposit. This friction is recognized as a major contributor to the total pressure drop in the slurry flow through a pipe with a stationary deposit.
    Permanent Link: http://hdl.handle.net/11104/0154964

     
     
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