123 - 132 |
Comparison of the performance of the LCVM model (an EoS/G(E) model) and the PHCT EoS (the Perturbed Hard Chain Theory Equation of State) in the prediction of the Vapor-Liquid Equilibria of binary systems containing light gases Boukouvalas CJ, Magoulas KG, Tassios DP, Kikic I |
133 - 139 |
High-pressure solubility data of the system resveratrol (3) plus ethanol (2) plus CO2 (1) Berna A, Chafer A, Monton JB |
141 - 148 |
Enzymatic alcoholysis of palm kernel oil in n-hexane and SCCO2 Oliveira D, Oliveira JV |
149 - 159 |
Mathematical modeling of extraction of egg yolk oil with supercritical CO2 Wu WZ, Hou YC |
161 - 175 |
Modeling and simulation of the supercritical CO2 extraction of vegetable oils Reverchon E, Marrone C |
177 - 185 |
Incorporation of disperse dye in N,N-dimethylacrylamide modified poly(ethylene terephthalate) fibers with supercritical CO2 Santos WLF, Porto MF, Muniz EC, Povh NP, Rubira AF |
187 - 198 |
Solubilities and diffusion coefficients of carbon dioxide in poly(vinyl acetate) and polystyrene Sato Y, Takikawa T, Takishima S, Masuoka H |
199 - 207 |
Attempt to explain the changes in solvation of polystyrene in supercritical CO2/ethanol mixtures using infrared and Raman spectroscopy Lalanne P, Rey S, Cansell F, Tassaing T, Besnard M |
209 - 215 |
Synthesis of barium titanate using supercritical CO2 drying of gels Novak Z, Knez Z, Ban I, Drofenik M |