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The model involves mass and momentum transport equations, which were solved for boundary conditions developed in the present study.
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The formulation of the two-fluid model involves the mass and momentum balance equations of each fluid averaged over the void cross-sectional area of the reactor, as well as an additional equation for the capillary pressure gradient deduced from a momentum balance analysis at the gas liquid interface.
The global modelling of the airlift involves mass and momentum equations for the three phases.
The vehicle model addresses vehicle suspension system, which involves mass distribution, dimension, and configuration of the vehicle.
Whatever the conditions, profiles were successfully modeled thanks to a coupling that involves mass transfer limitation between the fluid and the photocatalytic media and the degradation reaction happening for the adsorbed pollutant.
The other involves mass slaughter.
This model involves solving coupled mass and energy balances, and chemical potential equations using a genetic algorithm.
The model involves area-averaged mass and momentum balance equations of each fluid as well as an expression for the capillary pressure gradient deduced from a momentum balance analysis at the gas liquid interface.
A more detailed model involving simultaneous mass transfer, reduction and vapourization steps was formulated.
To study solute distribution at the solid liquid (S L) interface during melt crystallization, we examined the applicability of the interfacial solute distribution factor proposed based on a kinetic model involving both mass and heat balances at the interface.
The hydrogen electrode reaction (HER) in steady state was described through a model involving mechanistic, mass-transport, and acid base events.
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CEO of Professional Science Editing for Scientists @ prosciediting.com