| [1] | HURON M J,VIDAL J.New mixing rules in simpleequations of state for representing vaper-liquid equilibria ofstrong non-ideal mixture[J].Fluid Phase Equilibria.1979,3:255-267 | | [2] | WONG D S H,SANDLER S I.Theoretically correct mixingrule for cubic equations of state[J].AIChE J.1992,38:671-680 | | [3] | ORBEY H,SANDLER S I.On the combination of equationof state and excess free energy models[J].Fluid PhaseEquilibria,1995,111:53-70. | | [4] | LARSEN B L,RASMUSSEN P,FREDENSLUND A.Amodified UNIFAC group-contribution model for prediction ofphase equilibria and heats of mixing[J].Ind Eng ChemRes,1987,26:2 274-2 286. | | [5] | ORBEY H,SANDLER S I.A comparison of Huron-Vidaltype mixing rules for mixtures of compounds with large sizedifferences,and a new mixing rule[J].Fluid PhaseEquilibria,1997,132:1-14. | | [6] | FREDENSLUND A,GMEHLING J,RASMUSSEN P.Vapor-Liquid Equilibra Using UNIFAC��A Group Contribution[M].Amsterdam:Elsevier,1977. | | [7] | ��Ω��.��е���Ż����[M].��2��.����:�廪��ѧ������,1994. |
|
2006, Vol. 23 
