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    Pressure Losses and Limiting Reynolds Numbers for Non-Newtonian Fluids in Short Square-Edged Orifice Plates

    Source: Journal of Fluids Engineering:;2012:;volume( 134 ):;issue: 009::page 91204
    Author:
    Butteur Ntamba Ntamba
    ,
    Veruscha Fester
    DOI: 10.1115/1.4007156
    Publisher: The American Society of Mechanical Engineers (ASME)
    Abstract: Correlations predicting the pressure loss coefficient along with the laminar, transitional, and turbulent limiting Reynolds numbers with the β ratio are presented for short square-edged orifice plates. The knowledge of pressure losses across orifices is a very important industrial problem while predicting pressure losses in piping systems. Similarly, it is important to define stable operating regions for the application of a short orifice at lower Reynolds numbers. This work experimentally determined pressure loss coefficients for square-edged orifices for orifice-to-diameter ratios of β = 0.2, 0.3, 0.57, and 0.7 for Newtonian and non-Newtonian fluids in both laminar and turbulent flow regimes.
    keyword(s): Pressure , Fluids , Turbulence , Reynolds number AND Plates (structures) ,
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      Pressure Losses and Limiting Reynolds Numbers for Non-Newtonian Fluids in Short Square-Edged Orifice Plates

    URI
    https://yetl.yabesh.ir/yetl1/handle/yetl/149081
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    contributor authorButteur Ntamba Ntamba
    contributor authorVeruscha Fester
    date accessioned2017-05-09T00:51:10Z
    date available2017-05-09T00:51:10Z
    date copyrightSeptember, 2012
    date issued2012
    identifier issn0098-2202
    identifier otherJFEGA4-926053#091204_1.pdf
    identifier urihttp://yetl.yabesh.ir/yetl/handle/yetl/149081
    description abstractCorrelations predicting the pressure loss coefficient along with the laminar, transitional, and turbulent limiting Reynolds numbers with the β ratio are presented for short square-edged orifice plates. The knowledge of pressure losses across orifices is a very important industrial problem while predicting pressure losses in piping systems. Similarly, it is important to define stable operating regions for the application of a short orifice at lower Reynolds numbers. This work experimentally determined pressure loss coefficients for square-edged orifices for orifice-to-diameter ratios of β = 0.2, 0.3, 0.57, and 0.7 for Newtonian and non-Newtonian fluids in both laminar and turbulent flow regimes.
    publisherThe American Society of Mechanical Engineers (ASME)
    titlePressure Losses and Limiting Reynolds Numbers for Non-Newtonian Fluids in Short Square-Edged Orifice Plates
    typeJournal Paper
    journal volume134
    journal issue9
    journal titleJournal of Fluids Engineering
    identifier doi10.1115/1.4007156
    journal fristpage91204
    identifier eissn1528-901X
    keywordsPressure
    keywordsFluids
    keywordsTurbulence
    keywordsReynolds number AND Plates (structures)
    treeJournal of Fluids Engineering:;2012:;volume( 134 ):;issue: 009
    contenttypeFulltext
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