Phase equilibria of CO2 + dl-α-tocopherol at temperatures from 292 K to 333 K and pressures up to 26 MPa

Revision and summary of the group contribution equation of state parameter table: Application to edible oil constituents

“…9. Experimental and calculated equilibrium constant (k eq = weight fraction in vapor phase/weight fraction in liquid phase) for ethyloleate at (×) 313 K, (+) 323 K and (*) 333 K [36], triolein at (᭹) 313 K [35] and ( ) 333 K [37], ␣-tocopherol at ( ) 313 K [33] and ( ) 333 K [34], squalene at ( ) 313 K [31] in binary mixture with CO 2 . Solid lines: GC-EoS correlation.…”

Ternary-phase equilibria for CO2+3-methyl-1-butanol+2-phenylethanol

“…The apparatus used to perform the measurements presented here is the same as used for the measurements on the binary mixtures [7], and it has previously been described in detail [8,9]. The equilibrium cell is built around a sapphire cylinder, which allows full visual observation of its contents.…”

High pressure vapor–liquid equilibrium for the ternary system ethanol/(±)-menthol/carbon dioxide

“…The apparatus and methodology are described in detail elsewhere [12,13]. Temperature and pressure inside the cell were measured with the mercury thermometer (12) and temperature controller (13), and the pressure indicator P2, respectively. CO 2 was compressed with the compressor (C) and then fed to the cell (through valves V1-V3) to the desired pressure.…”