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- W2258376062 abstract "Considering the non-ideal behavior of uids and their eects on hydrodynamic and masstransfer in multiphase ow is very essential. Simulations were performed that take into account theeects of mass transfer and mixture non-ideality on the hydrodynamics reported by Bozorgmehry et al.In this paper, by assuming the density of phases to be constant and using Raoult's law instead of EOSand the fugacity coecient denition, respectively, for both liquid and gas phases, the importance of nonidealityeects on mass transfer and hydrodynamic behavior was studied. The results for a system ofoctane/propane (T = 323 K and P = 445 kPa) also indicated that the assumption of constant density insimulation had a major role to diverse from experimental data. Furthermore, comparison between obtainedresults and previous reports indicated signicant dierences between experimental data and simulationresults with more ideal assumptions." @default.
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- W2258376062 date "2010-06-01" @default.
- W2258376062 modified "2023-09-26" @default.
- W2258376062 title "IMPACT OF THERMODYNAMIC NON-IDEALITIES AND MASS TRANSFER ON MULTI-PHASE HYDRODYNAMICS" @default.
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