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This discrepancy between isotherm data and SHCS data is most likely due to the influence of mass transport on the binding kinetics obtained from the isotherm data of CTB binding to GM1.
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The equilibrium data are fitted into Langmuir and Freundlich equations to determine the correlation between the isotherm models and experimental data.
The discrepancy between the isotherm collected with a single solution of PnA and that collected with a quasi-continuous flow is particularly apparent at lower PnA concentrations.
The apparent isosteric enthalpy of adsorption (Qst) and entropy of adsorption (Δ S) as a function of loading for water vapour sorption on 1 and 2 were determined by linear regression between adjacent isotherm points for adsorption isotherms and are shown in Figure 4 c and d, respectively.
This paper presents comparison between sorption isotherms of a Jersey knitted fabric and frayed yarns which constitute.
The difference between sorption isotherms of the two samples, at high humidity, is explained by geometrical consideration.
The comparison between the isotherms of the nanofluid and pure water shows that in each point of the channel, the nanofluid temperature is higher than the pure water.
As the Ra number increases, the spacing between the isotherms adjacent to the heated and cooled walls further decreases, which is indicative of an increase in the heat transfer rate.
Furthermore, the difference between the isotherms could be related to the polymer microstructure, however, it suggested that a correction due to the difference between the surface and bulk microstructure is necessary for Nafion.
The behaviour of the system can be well predicted by a simple equilibrium stage model with concentration dependent distribution coefficients to account for non-linearity and coupling between the isotherms for the two components.
A strategy based on the correlation between adsorption isotherms and breakthrough performance was further proposed to simplify the column adsorption design using absorbents with small/uniform size and fast adsorption kinetics like Ca II -CS miCa II -CSs to cut down the gap between lab and industry.
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