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A statistical analysis of our experimental measurements suggests a power function correlation to model the liquid penetration length.
For verifying the proposed model, the liquid velocity distributions on a sieve tray were measured by the hot-film anemometry.
The modified quasi-chemical model in the pair approximation was used to model the liquid phase, while solid solutions were modeled using compound energy formalism.
In the proposed model, the liquid is assumed to be inviscid, incompressible and irrotational, and its motion is completely characterized by a velocity potential function.
Using the concentration polarization model, the liquid boundary layer thickness on the feed side and the intrinsic membrane permeance were calculated for various pervaporation systems.
In order to interpret these results Computational Fluid Dynamics (CFD) has been used to model the liquid flow within the packed sandwich structures.
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In the present proposed MFC modeling, the liquid phase and solid phase correspond to proton transfer and electron transfer, respectively.
So dynamic spectral analyses were carried out by modeling the liquid mass through its impulsive component only.
Thus, dynamic spectral analyses were carried out by modeling the liquid mass through its impulsive component only.
It consists of a lumped model for the liquid phase and a distributed model for the solid phase.
Modeling of membrane contactors as absorber units requires a rigorous absorption model where the liquid phase is discretized in the radial direction.
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