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Hence, the degradation of two-phase heat transfer due to mass diffusion resistance is not captured.
While the adsorption is controlled by mass diffusion resistance when (tth/tm)~O(1) or less.
It is though well known that the heat transfer coefficient of a refrigerant mixture can be reduced due to either mass diffusion resistance of the volatile component or an unfavourable change in the mixture transport properties [13, 14].
The model accounts for internal mass diffusion resistance, surface mass transfer resistance, external film heat transfer resistance, and heat transfer to the surrounding environment.
Internal resistance distribution shows that mass diffusion resistance of GAC-MFC is at least 50% lower than that of GG-MFC when the substrate COD is ∼50 mg/L, indicating that the adsorptive effect of granular activated carbon packed anode helps to effectively facilitate mass transfer at low COD concentrations.
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In the two-film model, gaseous molecules in the bulk phase diffuse through a gas liquid film and then are transferred into the bulk solution; therefore, the total resistance to mass transfer consists of diffusion resistance at the gas liquid interface and mass transfer resistance in liquid phase.
Model equations include film mass transfer, intra-particle diffusion resistance, axial dispersion for the outer fluid phase, plug flow of the solid phase and linear adsorption equilibrium of glucose/fructose.
General expressions for the first and second chromatographic moments of components and waves are given by taking into account axial dispersion, film mass transfer resistance, and intraparticle diffusion resistance for chromatographic column packed with inert core adsorbents.
In order to demonstrate their potential, different scenarios are considered to quantify the effects of the relative core size, axial dispersion, film mass transfer resistance and intraparticle diffusion resistance in the porous layer on the elution profiles.
The effects of the size of inert core, sample input mode, axial dispersion, film mass transfer resistance and intraparticle diffusion resistance, on the breakthrough and elution curves are discussed.
Reducing RH can result in slower electrode kinetics, including electrode reaction and mass diffusion rates, and higher membrane resistance.
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