107 - 120 |
Solubility in Supercritical-Fluid Mixtures with Cosolvents - An Integral-Equation Approach Tanaka H, Nakanishi K |
121 - 141 |
Prediction of the Solubility of Aromatic-Hydrocarbons in Supercritical CO2 with EOS/G(E) Models Spiliotis N, Magoulas K, Tassios D |
143 - 158 |
Computation of Compositional Grading in Hydrocarbon Reservoirs - Application of Continuous Thermodynamics Liragaleana C, Firoozabadi A, Prausnitz JM |
159 - 172 |
Equation of State for Hard-Sphere Chain Molecules Yu YX, Lu JF, Tong JS, Li YG |
173 - 179 |
Application of the Simplified Hole Theory Equation of State to Polymer-Solutions and Blends Zhong CL, Wang WC, Lu HZ |
181 - 203 |
Measurement and Prediction of 3-Phase Water/Hydrocarbon Equilibria Eubank PT, Wu CH, Alvarado JF, Forero A, Beladi MK |
205 - 210 |
Excess-Enthalpies of Binary-Mixtures Toluene Plus Propylbenzene, Plus Butylbenzeae and Plus Bexylbenzene at 298.15, 308.15 and 318.15 K Jain DV, Chadha R, Dhar NS |
211 - 255 |
Distribution of Acetic-Acid Between Water and Organic Solutions of Tri-N-Octylamine Ziegenfuss H, Maurer G |
257 - 273 |
Vapor-Liquid-Equilibrium Measurements and Data-Analysis of Isoprene and N-Pentane Mixture Lee LS, Huang JF, Yang WY, Chiang AS |
275 - 286 |
Vapor-Liquid-Equilibria in Nonpolar Mixtures .3. Binary-Mixtures of Alkylbenzenes and N-Alkanes at 313.15 K Goral M |
287 - 292 |
High-Pressure 3-Phase Equilibria for the Carbon-Dioxide Ethanol-Water System Yoon JH, Lee H, Chung BH |
293 - 303 |
Excess Molar Volumes of Binary-Mixtures of Toluene and Ethylbenzene with Propylbenzene, Butylbenzene and Hexylbenzene at 298.15, 308.15 and 318.15 K Jain DV, Dhar NS |
305 - 315 |
Densities and Excess Molar Volumes of 8 N-Alkane Binary-Systems at 293.15 and 298.15 K Wu JN, Asfour AF |