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Capillary pressure and relative permeabilities (k_{beta}), (beta=l,g), are usually posed as a function of the liquid saturation (S_{l}).
The solid composition is first obtained as a function of the liquid composition by determining the saddle point of the island formation energy.
A model is derived to calculate the liquid hold-up inside the monolith as a function of the liquid circulation flow rate.
An experimental investigation was carried out to characterize the mass transfer in the packing of the cooling tower as a function of the liquid and gas flow rates, whose results were within the range of the measurement accuracy.
This paper presents a hydrodynamic study performed in a bench scale column, where the axial dispersion and the liquid holdup, as a function of the liquid flow rate, are estimated using residence time distribution experiments.
The experimental data were used together with available literature data in the development of a dimensionless correlation for predicting the critical velocity as a function of the liquid properties.
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Vapor-like second mixture calculations are initiated by calculating the mixture fugacity ((f_{{{text{ci}}_{text{o}}}})) as a function of the liquid-phase pressure and overall composition ((c_{i})) as shown in Eq. (1).
A numerical solution for the liquid-phase Sherwood number was obtained as a function of the liquid-phase Reynolds and Schmidt numbers, the angle of inclination of the wetted-wall plate and the dimensionless distance in flow direction.
Correlation of dynamic contact angles as a function of the capillary number in liquid-liquid-solid systems is important in a number of applications.
The dynamic viscosities of the liquids are respectively 0.73, 4, 12.3, 17.5, and 31.2 mPa.s at 25°C. Figure 5 shows the evolution of the PL peak position as a function of the dynamic viscosity of the liquids at 300 K.
The flow rate limitation can then be investigated as a function of the channel geometry as well as liquid property based on the model.
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