Compressed liquid densities and excess molar volumes for (CO2+1-pentanol) binary system at temperatures from 313 to 363K and pressures up to 25MPa

Estimating the liquid properties of 1-alkanols from C5 to C12 by FT-EoS and CP-PC-SAFT: Simplicity versus complexity

“…Lines -modeling of CP-PC-SAFT with k 12 = 0.057, l 12 = 0.012. Literature data: VLE[79][80][81][82][83], densities[83,84].…”

Solubilities Prediction and Partial Molar Volume Calculation for 2-Butanol and CO₂ Binary Mixture at High Pressure

“…C. Derived partial molar volume at equilibrium state By binary interation parameters obtained from PR-EOS, according to equation (6)(7)(8)(9), partial molar volumes of CO 2 and 2-butanol in vapor and liquid phase at equilibrium were evaluated, and the results were presented in tab.4.…”

“…Alcohol which exists widely in fermentation wasted water is often used as entrainer to control the polarity of supercritical fluid, or as a modifier in supercritical fluid chromatography. Thus, the study on supercritical CO 2 and alcohol is more and more popular [5][6][7][8][9][10] .. Thermodynamical knowledge of phase equilibrium in high pressures CO 2 under the work temperatures is very important. It is required for engineering application such as in the design, simulation, optimization and operation of separation processes.…”