Abstract:Currently, there is a great interest in the production of biofuels such as biodiesel, bioethanol and biobutanol. These processes involve liquidÀliquid equilibria, which are important for the overall design of the process. However, suitable experimental data are often scarce. The Cosmo-SAC model provides a method to predict liquidÀliquid equilibrium data from quantum chemical calculations without any experimental data. Hence, it can be used to provide initial estimates where experimental data are not available.… Show more
“…However, the COSMO-SAC model predicts LLE experiments requiring only initial feed point data, which saves the experiment time and difficulty. Previously, many papers reported prediction of LLE experiments using COSMO-SAC model and achieved good results. ,, On the basis of COSMO-SAC theory, the activity factor of solute i in solvent S (γ i/S ) can be calculated bywhere Δ G * res denotes the restoring free energy from the chemical potential of segment in the COSMO-RS model, γ i/S SG is calculated by the Staverman–Guggenheim combinatorial term.…”
Section: Resultsmentioning
confidence: 99%
“…Hydrogen-bonding atoms were defined as nitrogen, oxygen, fluorine atoms, and hydrogen atoms combined with oxygen, nitrogen, fluorine atoms in a pure substance, and others were non-hydrogen bond atoms . A detailed description of COSMO-SAC model was published in refs. ,,,, …”
Methyl isobutyl ketone (MIBK) had been successfully employed to extract phenols from coal gasification wastewater since 2009, and it has been proved to be an excellent extraction solvent. In this work, the liquid−liquid equilibrium (LLE) data were measured for the ternary systems MIBK + 2,3-/3,4-/3,5dimethylphenol + water from 298.15 to 343.15 K. High partition coefficient and separation factor indicated that MIBK could extract dimethylphenols from an aqueous solution well. The Hand equation and the Bachman equation were used for testing the consistency of the determined tie-line data. The NRTL and UNIQUAC thermodynamic models were utilized to correlate these measured LLE data, and their root-mean-square deviations did not exceed 0.5%. The conductor-like screening model for segment activity coefficient was employed to predict the LLE data. Results showed that the prediction values are close to the measured data.
“…However, the COSMO-SAC model predicts LLE experiments requiring only initial feed point data, which saves the experiment time and difficulty. Previously, many papers reported prediction of LLE experiments using COSMO-SAC model and achieved good results. ,, On the basis of COSMO-SAC theory, the activity factor of solute i in solvent S (γ i/S ) can be calculated bywhere Δ G * res denotes the restoring free energy from the chemical potential of segment in the COSMO-RS model, γ i/S SG is calculated by the Staverman–Guggenheim combinatorial term.…”
Section: Resultsmentioning
confidence: 99%
“…Hydrogen-bonding atoms were defined as nitrogen, oxygen, fluorine atoms, and hydrogen atoms combined with oxygen, nitrogen, fluorine atoms in a pure substance, and others were non-hydrogen bond atoms . A detailed description of COSMO-SAC model was published in refs. ,,,, …”
Methyl isobutyl ketone (MIBK) had been successfully employed to extract phenols from coal gasification wastewater since 2009, and it has been proved to be an excellent extraction solvent. In this work, the liquid−liquid equilibrium (LLE) data were measured for the ternary systems MIBK + 2,3-/3,4-/3,5dimethylphenol + water from 298.15 to 343.15 K. High partition coefficient and separation factor indicated that MIBK could extract dimethylphenols from an aqueous solution well. The Hand equation and the Bachman equation were used for testing the consistency of the determined tie-line data. The NRTL and UNIQUAC thermodynamic models were utilized to correlate these measured LLE data, and their root-mean-square deviations did not exceed 0.5%. The conductor-like screening model for segment activity coefficient was employed to predict the LLE data. Results showed that the prediction values are close to the measured data.
“…Second, calculate the activity coefficients of each pure compound and mixture by using the σ-profile p(σ). The details of the COSMO-SAC model can be found in other publications [32,40,41] and in the Appendix. The COSMO-SAC universal parameter for the effective contact area a eff in this work is 6.55Å 2 , while the hydrogen bonding coefficient c hb is 100 kcalÅ 4 mol -1 e -2 .…”
In this work, liquid-liquid equilibrium (LLE) data for the ternary systems, mesityl oxide + o-, m-, p-cresol + water, were determined at 333.2 K and 353.2 K under 101 kPa. The high distribution coefficient and selectivity calculated by the experimental tie-line data indicate excellent efficiency for mesityl oxide extracting cresols from aqueous solutions. The NRTL and UNIQUAC models were used to correlate the experimental LLE data, with root mean square deviations (RMSDs) below 2.1% and 1.5%, respectively. The COSMO-SAC model was also employed to calculate the LLE data, which agreed with the experimental results quite well.
“…They have been applied to a wide range of compounds ranging from simple nonpolar solvents to ionic liquids [35][36][37][38][39][40][41][42] and have shown significant promise in prediction of phase equilibria of these compounds. However, the application of these models to polymer phase equilibria is scarce [43,44], mainly because the quantum chemical calculations for polymers are computationally very intensive.…”
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