137 - 145 |
Vapor-liquid equilibrium of nitrogen in an equimolar hexane plus decane mixture at temperatures of 258, 273, and 298 K and pressures to 20 MPa Uribe-Vargas V, Trejo A |
147 - 151 |
Solubility of titanocene dichloride in supercritical propane Wang JD, Chen JZ, Yang YR |
153 - 160 |
Effect of oxyethylene groups on the behaviour of thermodynamic properties of pyrrolidin-2-one and poly(ethylene glycols) Mehta SK, Ram G, Sharma AK |
161 - 165 |
Isothermal vapour-liquid equilibria in the binary and ternary systems composed of 2-propanol, diisopropyl ether and 1-methoxy-2-propanol Psutka S, Wichterle I |
167 - 169 |
Thermodynamic modeling of the solubilities of fatty acids in supercritical fluids Madras G |
171 - 180 |
A new spline approach for data fitting Nunhez JR, Costa CBB, Guirardello R |
181 - 188 |
Measurement of binary diffusion coefficient from impulse response curve having extremely low absorbance intensity under supercritical condition by noise elimination technique Funazukuri T, Kong CY, Kagei S |
189 - 198 |
Interaction parameters for multi-component aromatic extraction with sulfolane Ahmad SA, Tanwar RS, Gupta RK, Khanna A |
199 - 209 |
The electrolyte NRTL model and speciation approach as applied to multicomponent aqueous solutions of H2SO4, Fe-2(SO4)(3), MgSO4 and Al-2(SO4)(3) at 230-270 degrees C Haghtalab A, Papangelakis VG, Zhu XT |
211 - 223 |
Prediction of thermodynamic derivative properties of natural condensate gases at high pressure by Monte Carlo simulation Lagache MH, Ungerer P, Boutin A |