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    Friction Factor Correlations for Gas Flow in Slip Flow Regime

    Source: Journal of Fluids Engineering:;2007:;volume( 129 ):;issue: 010::page 1268
    Author:
    Chungpyo Hong
    ,
    Stephen E. Turner
    ,
    Mohammad Faghri
    ,
    Yutaka Asako
    DOI: 10.1115/1.2776966
    Publisher: The American Society of Mechanical Engineers (ASME)
    Abstract: Poiseuille number, the product of friction factor and Reynolds number (fRe) for quasi-fully-developed gas microchannel flow in the slip flow regime, was obtained numerically based on the arbitrary-Lagrangian-Eulerian method. Two-dimensional compressible momentum and energy equations were solved for a wide range of Reynolds and Mach numbers for constant wall temperatures that are lower or higher than the inlet temperature. The channel height ranges from 2 μm to 10 μm and the channel aspect ratio is 200. The stagnation pressure pstg is chosen such that the exit Mach number ranges from 0.1 to 1.0. The outlet pressure is fixed at atmospheric conditon. Mach and Knudsen numbers are systematically varied to determine their effects on fRe. The correlation for fRe for the slip flow is obtained from that of fRe of no-slip flow and incompressible theory as a function of Mach and Knudsen numbers. The results are in excellent agreement with the available experimental measurements. It was found that fRe is a function of Mach and Knudsen numbers and is different from the values by 96/(1+12Kn) obtained from the incompressible flow theory.
    keyword(s): Flow (Dynamics) , Mach number , Friction , Temperature , Channels (Hydraulic engineering) , Pressure , Equations , Slip flow , Gas flow , Compressibility , Poiseuille flow , Wall temperature AND Reynolds number ,
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      Friction Factor Correlations for Gas Flow in Slip Flow Regime

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    contributor authorChungpyo Hong
    contributor authorStephen E. Turner
    contributor authorMohammad Faghri
    contributor authorYutaka Asako
    date accessioned2017-05-09T00:24:00Z
    date available2017-05-09T00:24:00Z
    date copyrightOctober, 2007
    date issued2007
    identifier issn0098-2202
    identifier otherJFEGA4-27274#1268_1.pdf
    identifier urihttp://yetl.yabesh.ir/yetl/handle/yetl/135911
    description abstractPoiseuille number, the product of friction factor and Reynolds number (fRe) for quasi-fully-developed gas microchannel flow in the slip flow regime, was obtained numerically based on the arbitrary-Lagrangian-Eulerian method. Two-dimensional compressible momentum and energy equations were solved for a wide range of Reynolds and Mach numbers for constant wall temperatures that are lower or higher than the inlet temperature. The channel height ranges from 2 μm to 10 μm and the channel aspect ratio is 200. The stagnation pressure pstg is chosen such that the exit Mach number ranges from 0.1 to 1.0. The outlet pressure is fixed at atmospheric conditon. Mach and Knudsen numbers are systematically varied to determine their effects on fRe. The correlation for fRe for the slip flow is obtained from that of fRe of no-slip flow and incompressible theory as a function of Mach and Knudsen numbers. The results are in excellent agreement with the available experimental measurements. It was found that fRe is a function of Mach and Knudsen numbers and is different from the values by 96/(1+12Kn) obtained from the incompressible flow theory.
    publisherThe American Society of Mechanical Engineers (ASME)
    titleFriction Factor Correlations for Gas Flow in Slip Flow Regime
    typeJournal Paper
    journal volume129
    journal issue10
    journal titleJournal of Fluids Engineering
    identifier doi10.1115/1.2776966
    journal fristpage1268
    journal lastpage1276
    identifier eissn1528-901X
    keywordsFlow (Dynamics)
    keywordsMach number
    keywordsFriction
    keywordsTemperature
    keywordsChannels (Hydraulic engineering)
    keywordsPressure
    keywordsEquations
    keywordsSlip flow
    keywordsGas flow
    keywordsCompressibility
    keywordsPoiseuille flow
    keywordsWall temperature AND Reynolds number
    treeJournal of Fluids Engineering:;2007:;volume( 129 ):;issue: 010
    contenttypeFulltext
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