Authors: VOUTSAS EC SPILIOTIS N KALOSPIROS NS TASSIOS D

Citation: Ec. Voutsas et al., PREDICTION OF VAPOR-LIQUID-EQUILIBRIA AT LOW AND HIGH-PRESSURES USINGUNIFAC-BASED MODELS, Industrial & engineering chemistry research, 34(2), 1995, pp. 681-687

Authors: BOUKOUVALAS C SPILIOTIS N COUTSIKOS P TZOUVARAS N TASSIOS D

Citation: C. Boukouvalas et al., PREDICTION OF VAPOR-LIQUID-EQUILIBRIUM WITH THE LCVM MODEL - A LINEARCOMBINATION OF THE VIDAL AND MICHELSEN MIXING RULES COUPLED WITH THE ORIGINAL UNIFAC AND THE T-MPR EQUATION OF STATE, Fluid phase equilibria, 92, 1994, pp. 75-106

Authors: SPILIOTIS N MAGOULAS K TASSIOS D

Citation: N. Spiliotis et al., PREDICTION OF THE SOLUBILITY OF AROMATIC-HYDROCARBONS IN SUPERCRITICAL CO2 WITH EOS G(E) MODELS/, Fluid phase equilibria, 102(2), 1994, pp. 121-141

Authors: SPILIOTIS N BOUKOUVALAS C TZOUVARAS N TASSIOS D

Citation: N. Spiliotis et al., APPLICATION OF THE LCVM MODEL TO MULTICOMPONENT SYSTEMS - EXTENSION OF THE UNIFAC INTERACTION PARAMETER TABLE AND PREDICTION OF THE PHASE-BEHAVIOR OF SYNTHETIC GAS CONDENSATE AND OIL SYSTEMS, Fluid phase equilibria, 101, 1994, pp. 187-210