1991
DOI: 10.1063/1.857855
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Steady, isentropic flows of dense gases

Abstract: Steady isentropic flows of fluids in their dense gas regime are examined. It is shown that the Mach number may increase, rather than decrease, with density or pressure if the specific heats of the fluid are sufficiently large. Conditions are also reported under which isentropic expansions through converging–diverging nozzles are not possible, regardless of the imposed exit pressure. In such cases, the nozzle must be replaced with one having multiple throats. Applications to external transonic flows are briefly… Show more

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Cited by 59 publications
(45 citation statements)
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“…Only HMC fluids may possibly feature a nonmonotonous Mach number variation with density in a limited thermodynamic region. 25,26 This is not the case for the thermodynamic conditions considered here.…”
Section: -9mentioning
confidence: 69%
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“…Only HMC fluids may possibly feature a nonmonotonous Mach number variation with density in a limited thermodynamic region. 25,26 This is not the case for the thermodynamic conditions considered here.…”
Section: -9mentioning
confidence: 69%
“…For HMC fluids also qualitative differences in fluid dynamic behavior can be observed in the dense-gas region, close to saturation. [25][26][27] Most notable is the increase in the speed of sound upon isentropic expansion, possibly leading to a local decrease in the Mach number, 11,27-29 which instead increases 33 may possibly occur, although no experimental evidence of these "exotic" wave fields is available yet. 34 In Ref.…”
Section: ͑6͒mentioning
confidence: 99%
“…In summary, the RKS model in non-dimensional form (5), (8) considered in the present work depends on three uncertain parameters, namely the acentric factor ω, the exponent n and the reduced ideal-gas constant-volume specific heat at the critical temperature c v,∞ (T c ).…”
Section: Rks Modelmentioning
confidence: 99%
“…Globally, the MAH thermodynamic model in reduced form, Eq. (11) and (8), requires the knowledge of six material-dependent parameters, namely, the critical pressure p c , the critical temperature T c , the critical compressibility factor Z c , the normal boiling temperature T b , the exponent n and the reduced ideal-gas constant-volume specific heat at the critical temperature c v,∞ (T c ). Nevertheless, previous results [13] show that Z c , T b and n have a relatively small impact on the results.…”
Section: Zcmentioning
confidence: 99%
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