1998
DOI: 10.1016/s0017-9310(98)00049-0
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Isolated fluid oxygen drop behavior in fluid hydrogen at rocket chamber pressures

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Cited by 104 publications
(43 citation statements)
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“…Thus, the density ratio may be well below the 0(103) that characterizes its liquid/gas value, but the measurement will still identify a change in the index of refraction providing that the change is sudden (steep gradients). As shown by simulations of supercritical fluids (see Harstad and Bellan [7]), the density gradients may remain large during the initial stage of two supercritical fluids mixing, thus making them optically identifiable. Therefore, there is no inconsistency between the optical observation of 'drops' and 'ligaments' and the fluids (injected and surrounding) being both in a supercritical state.…”
Section: Experimental Observationsmentioning
confidence: 99%
“…Thus, the density ratio may be well below the 0(103) that characterizes its liquid/gas value, but the measurement will still identify a change in the index of refraction providing that the change is sudden (steep gradients). As shown by simulations of supercritical fluids (see Harstad and Bellan [7]), the density gradients may remain large during the initial stage of two supercritical fluids mixing, thus making them optically identifiable. Therefore, there is no inconsistency between the optical observation of 'drops' and 'ligaments' and the fluids (injected and surrounding) being both in a supercritical state.…”
Section: Experimental Observationsmentioning
confidence: 99%
“…The viscosity, the Schmidt number (Sc = μ/(ρα D D)) and the Prandtl number (P r = μC p /(mλ)) were calculated from high-pressure single-species transport properties using mixing rules, as in Harstad & Bellan (1998). The calculated values were correlated, as summarized in table 2, and these correlations are then used to compute the transport properties μ, D and λ.…”
Section: Transport Coefficientsmentioning
confidence: 99%
“…This particular region is chosen for two primary reasons: (1) The PR EOS was found to be highly accurate within this region when compared to the more accurate model of Harstad et al (1997) with the relative error being in no case greater than approximately 1% for both the entropy and enthalpy predictions (this error can be larger than 25% at p = 6 MPa and T = 350 K). (2) Contour plots (not shown) of the viscosity, and of the Schmidt (Sc) and Prandtl (P r) numbers based on accurate species transport properties calculated as in Harstad & Bellan (1998), revealed that the viscosity is predominantly a function of T alone, whereas Sc and P r are predominantly functions of the mass fraction. This leads to the relatively simplified diffusion coefficients 28) where µ R is a reference viscosity and the reference temperatures T 1 and T 2 correspond to the free-stream temperatures for mixing layer simulations.…”
Section: Equation Of Statementioning
confidence: 99%