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Mass transfer model was established based on surface renewal model.
A one-dimensional heat transfer model was also developed to predict the R-values.
Then, a porosity-related mass transfer model was developed to theoretically simulate the urea transport.
The radiation transfer model was established to obtain the optical performance of the filter.
The heat and mass transfer model was validated against experimental results.
An adoptive transfer model was used to test whether Her2-S-Fab can inhibit tumor growth in vivo.
A radiative transfer model was used for calculating the diffuse PAR for cloudless sky conditions.
A pseudo-homogeneous mass transfer model was used to predict single-particle dissolution rates.
For more accurate engineering calculations, roll speed was calculated for continuous rolling and an approximate heat transfer model was proposed.
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The mass-transfer model was coupled with an available interfacial area model, yielding a dimensionless expression for the mass-transfer rate coefficient.
A mass-transfer model was proposed to predict the time profiles of Cu2+ during a simultaneous extraction stripping process in two hollow-fiber contactors.
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