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Engineering
Materials and Chemical Engineering
Modelling of two phase flow in packed bed using conservation equations
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[QUOTE="Chestermiller, post: 6586248, member: 345636"] I'm not so sure it is unreasonable to treat the liquid phase as ideal. This would certainly simplify things greatly. I suggest checking the literature relating to the VLE behavior of O2-N2 liquid mixtures and the activity coefficients for such mixtures. There is certainly going to be data on the activity coefficients for O2 and N2 in the vapor phase. Also, maybe the Lewis-Randle rule applies to the vapor. Spend some time digging in the literature. Once you have the non-ideal PVT behavior of the vapor mixtures, you can, knowing the ideal gas heat capacities of N2 and O2 vapor as a function of temperature, get the non-ideal variations in enthalpy with temperature and pressure. [/QUOTE]
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Materials and Chemical Engineering
Modelling of two phase flow in packed bed using conservation equations
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