2004
DOI: 10.1016/j.cryogenics.2004.02.008
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Two-phase flow of solid hydrogen particles and liquid helium

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Cited by 30 publications
(9 citation statements)
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“…Analogous to thermodynamic temperature in a gas, granular temperature for solid phase can be defined as [20]: (7) hereis the mean square of fluctuation velocity of particles, c= u s − . The transport equation for granular temperature based on conservation of particles fluctuating energy is given by [21]: (8) The first term on the right-hand side of this equation represents rates of production of pseudo-thermal energy by shear; the second represents diffusive transport of pseudo-thermal energy. γ Θsi represents dissipation of pseudo-thermal energy through inelastic collisions, φ fsi denotes exchange of fluctuating energy between fluid and i th component of solid phase, D fsi is granular energy dissipation rate, K Θsi is granular conductivity.…”
Section: Constitutive Equation Of Solid Phasementioning
confidence: 99%
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“…Analogous to thermodynamic temperature in a gas, granular temperature for solid phase can be defined as [20]: (7) hereis the mean square of fluctuation velocity of particles, c= u s − . The transport equation for granular temperature based on conservation of particles fluctuating energy is given by [21]: (8) The first term on the right-hand side of this equation represents rates of production of pseudo-thermal energy by shear; the second represents diffusive transport of pseudo-thermal energy. γ Θsi represents dissipation of pseudo-thermal energy through inelastic collisions, φ fsi denotes exchange of fluctuating energy between fluid and i th component of solid phase, D fsi is granular energy dissipation rate, K Θsi is granular conductivity.…”
Section: Constitutive Equation Of Solid Phasementioning
confidence: 99%
“…Recently, many researchers used a mixture model, a simplified form of the Eulerian approach, to predict concentration and velocity distributions as well as pressure drop of slurry flow [6][7][8]. Its computation is relatively inexpensive and it is straightforward to introduce a turbulence model into the mixture model [8]. However, the mixture model does not account for effects of particle-particle interaction which extensively occur at high solid loading, so it is reasonably accurate for slurries with moderate volumetric concentrations.…”
Section: Introductionmentioning
confidence: 99%
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“…There are commonly four popular approaches for numerically studying nanofluids: the single-phase model [6,7], the mixture multiphase model [8][9][10][11][12][13][14][15][16][17][18][19][20][21], the EulerianEulerian multiphase model [22][23][24][25][26][27] and the Euler-Lagrange multiphase model [28][29][30][31]. Although a variety of modified models that describe the heat transfer process in nanofluids is continually presented, thus far all modeling results are not very satisfactory: they all underestimate heat transfer coefficients when compared with experiment.…”
Section: Introductionmentioning
confidence: 99%
“…Once the size, shape, and volume fraction of the solid particles in the liquid carrier are known, it is easy to characterize the flow behavior in pipes theoretically. 8 Liquid droplet ejections from a fixed orifice have been previously studied in a variety of applications, ranging from the production of spherical nuclear fuel particles 9 to fuel injection into jet engines, 9 as well as inkjet printers. 10 However, there has been a lack of systematic experimental and theoretical studies of droplet injection from vibrating orifices for cryogenic fluids, perhaps due to the extremely complex nature of the problem.…”
Section: Introductionmentioning
confidence: 99%