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Table 2 shows Langmuir, Freundlich, Sips and Redlich Peterson isotherm constants obtained after fitting equilibrium concentration and adsorption capacity values into the models.
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Langmuir and Freundlich isotherm models were used to fit equilibrium data for OMC.
In addition, isothermal data were used to screen all the relevant adsorption isotherms models and the Temkin model was confirmed as the more effective to accurately fit equilibrium data for any of the considered different dye types.
Prediction of all fitted equilibrium constants using regressed values for ΔΩr,m and log K ii,m (Equation 15 and 17) substituted into Equation 14 yield an average log K θ = 0.2 ± 0.7 (1σ).
K12 is the fitted equilibrium dissociation constant for I1 with the binary complex of enzyme and I2.
This leads to currently unverifiable and potentially poor predictions of VZV dynamics beyond the fitted equilibrium states.
The calculation procedure described in this work may be used for the adjustment of reaction equilibrium constants by fitting the equilibrium model also to experimentally measured heats of absorption data in addition to PCO2 data.
The diffusion mechanism was analysed with intraparticulate diffusion model, while the equilibrium adsorption behaviour was analysed by fitting the equilibrium data with six isotherm models.
A correction of extrapolation errors was determined by fitting binary equilibrium data to the IAS theory.
Defluoridation capacity of nano γ-alumina was further investigated by fitting the equilibrium data to various isotherm as well as kinetic models.
This was carried out by fitting the equilibrium data to the Langmuir, Freundlich, Temkin, Dubinin Radushkevich, Sips, Vieth Sladek, Brouers Sotolongo and Radke Prausnitz isotherms.
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