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In this system, it was shown that mass transfer by chemical reaction with free chlorine generated in the anode was the dominant effect with physical mass transfer modelled as only contributing between 2.5% and 9% removal.
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Mass transfer model was established based on surface renewal model.
In the calculation of the mass transfer coefficients, different mass transfer models were implemented.
Moreover, the heat transfer or mass transfer models are special cases of the heat and mass transfer model in this paper.
Mass transfer models for the different flow patterns are proposed based on previous mass transfer coefficient models.
Ammonothermal systems are modeled using fluid dynamics and heat and mass transfer models.
The air conditions throughout the RHMX were obtained by a heat and mass transfer model.
An unsteady state mass transfer model has been developed for rotating disk ultrafiltration module.
This is done for each of the alternative mass transfer models.
This finding should cause concern regarding the validity of existing mass transfer models.
Then, a porosity-related mass transfer model was developed to theoretically simulate the urea transport.
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