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The dynamic response of the anode was analysed in terms of a substrate mass transport model.
We show that the temperature profile is modified when using the detailed mass transport model.
A detailed chemical equilibrium heat and mass transport model for porous ablators is presented for the first time.
Furthermore, a mass transport model was developed to accurately describe the kinetics of cell release results for each capsule.
The enabling feature of controlled evaporation by design of solution properties is verified by a simple mass transport model.
The heat and mass transport model was created using the numerical simulation modeling software for subsurface flow and transport processes FEFLOW 6.0.
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In the second part of the chapter, electrochemical kinetics and mass transport models are reviewed.
Processing conditions were optimized with the assistance of heat and mass transport modeling.
The mass transport modelling results depict the likely total petroleum hydrocarbon migration pattern in the worst-case scenario.
The two-phase mass transport models take account the effect of non-equilibrium evaporation/ condensation at the gas-liquid interface.
This paper presents state of the art mass transport models applied to PEME, a detailed literature review of these models and associate methods have been conducted.
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