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Likely because of this fact the adsorption kinetic was limited by liquid film mass transfer diffusion.
It is known that adsorption process could be controlled with different kinds of mechanisms, such as mass transfer, diffusion control, chemical reactions and particle diffusion.
Mass transfer, diffusion, adsorption and photochemistry are figured out to be the controlling mechanisms for photocatalytic degradation of volatile organic compounds (VOCs) using nano-TiO2 catalyst.
Referring once again to the results of Table 2, the resistance to the mass transfer diffusion across the liquid film could not be neglected for some adsorbents and initial concentrations of chromate.
By making these assumptions, the overall output concentration and system-theoretic models are determined by mass transfer (diffusion) of the information molecules and the surface nanopores/receptors/enzyme kinetics.
The results of the aforementioned models (not reported) showed that adsorption kinetic was not wholly controlled by the intra-particle diffusion or by the liquid film mass transfer diffusion.
Similar(43)
Two mass transfer-diffusion models were used to simulate the unsteady-state oxygen mass transport in the system.
Electrochemical impedance and polarization curve indicate that mass-transfer (diffusion) dominates the discharge capacity during high-rate discharge.
Multiple tests were performed to obtain the most favorable operating conditions to minimize mass-transfer diffusion limitations in the experiments.
The use of a mass-transfer operator generalizing all kinds of mass-transfer (diffusion, convection, thin layer, etc).
The slow progression toward complete desorption is consistent with previous findings of mass-transfer diffusion limitations on contaminant release at this site.
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