2007
DOI: 10.1007/s10404-007-0158-3
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Tangential momemtum accommodation in microtube

Abstract: International audienceExperimental investigations of isothermal steady flows for various gases have been carried out in a silica micro tube. This study is focused on the mass flow rate measurements of these flows in slip regime using a suitable powerful platform. First we analyse, for each gas, the pertinence of a first or second order continuum treatment ; then we deduce from experiments, using the appropriate treatment, the tangential momentum accommodation coefficient (TMAC) of each gas. The TMAC obtained f… Show more

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Cited by 88 publications
(58 citation statements)
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“…3. Our results do not show a clear correlation between the TMAC and the molecular mass of the gas, as reported in some studies, [21][22][23] and disputed by others. 20, 34 4.…”
Section: Discussioncontrasting
confidence: 88%
See 2 more Smart Citations
“…3. Our results do not show a clear correlation between the TMAC and the molecular mass of the gas, as reported in some studies, [21][22][23] and disputed by others. 20, 34 4.…”
Section: Discussioncontrasting
confidence: 88%
“…In flow rate measurements utilizing micro-tubes, [21][22][23] an inverse dependence of α on the molecular mass (proportional to m m ) has been observed. This dependence has been disputed in Refs.…”
Section: B Slip and Accommodation Coefficientsmentioning
confidence: 95%
See 1 more Smart Citation
“…Measurements of α u are typically performed by tracking the flow of gas through a microchannel. These experiments [38][39][40][41][42][43][44][45][46] are performed over a wide range of pressures at room temperature, and use microchannels with different shapes and diameters, constructed of various materials and surface treatments. Since the α u of each gas remains roughly constant across different conditions and flow regimes, it is justified to use the mean value of α u for each gas in the simulations.…”
Section: Simulation Parametersmentioning
confidence: 99%
“…The momentum accommodation coefficient depends on the type of fluid and wall material, and usually is selected from the range of 0.7 < f <1.0 (Duan and Muzychka, 2007;Ewart et al, 2007).…”
Section: Model Of Fluid In Boundary Layermentioning
confidence: 99%