2014
DOI: 10.1016/j.powtec.2014.02.005
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Numerical prediction of fully-suspended slurry flow in horizontal pipes

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Cited by 69 publications
(55 citation statements)
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References 44 publications
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“…The eddy viscosity, ν t , was evaluated by an extension of the standard high-Reynolds form of the k-ε model of Launder and Spalding (1974) to two-phase flows, which is well documented in Messa et al (2013Messa et al ( , 2014Messa et al ( , 2015.…”
Section: Methodology Governing Equationsmentioning
confidence: 99%
“…The eddy viscosity, ν t , was evaluated by an extension of the standard high-Reynolds form of the k-ε model of Launder and Spalding (1974) to two-phase flows, which is well documented in Messa et al (2013Messa et al ( , 2014Messa et al ( , 2015.…”
Section: Methodology Governing Equationsmentioning
confidence: 99%
“…7). The analysis is reported in Messa (2013) and Messa et al (2014), and revealed that the model is suitable for application to fully-suspended flows but not to bed flows, when the particles accumulate at the bottom of the pipe. Moreover, the model suffers from the absence of the near-wall lift force in the generalized drag term, since an expression of this force in case of dense slurries suitable for inclusion in a two-fluid model does not seem available at present.…”
Section: Supplementary Materials Appendix A: Validation Of the Model Imentioning
confidence: 99%
“…In Messa et al ( , 2014 we addressed horizontal pipe flows and found that the application of the equilibrium wall function of Launder and Spalding (1972) to model the velocity of the two phases, the turbulent kinetic energy and its dissipation rate in the near-wall cells procures reliable predictions of the viscous and mechanical contributions to friction (Shook and Bartosik, 1994). In order to generalize this result to a flow in which the equilibrium assumption is not satisfied, in this work we replaced the equilibrium wall function with the non-equilibrium one (Launder and Spalding, 1974).…”
Section: Computational Domain and Boundary Conditionsmentioning
confidence: 99%
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“…Amongst the main issues one can point out numerical instabilities, very timeconsuming, difficulty in dealing with the complex geometries since the calculation time becomes prohibitively expensive and none of the existing models has shown to be able to determine the minimum in the pressure gradient versus slurry velocity, which characterizes the transition to bed flows (Messa, Malin & Malavasi, 2014).…”
Section: Euler-euler Numerical Modelsmentioning
confidence: 99%