CALCULATING CRITICAL TRANSITIONS OF FLUID MIXTURES - THEORY VS EXPERIMENT

被引:81
作者
SADUS, RJ
机构
[1] Dept. of Computer Science, Swinburne University of Technology, Hawthorn, Victoria
关键词
D O I
10.1002/aic.690400810
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The progress in predicting critical transitions in fluid mixtures is reviewed. The critical state provides a valuable insight into the general phase behavior of a fluid and is closely linked with the nature and strength of intermolecular interaction. Calculations of critical equilibria have been confined mainly to binary mixtures. The prediction of binary gas-liquid critical properties was initially limited to empirical correlations. These techniques have been superseded by rigorous calculations of the critical conditions using realistic models of the fluid or equations of state. All of the known types of critical phenomena exhibited by binary mixtures can be, at least, qualitatively calculated. If an optimal combining rule parameter is allowed, continuous gas-liquid properties can be calculated accurately for a wide variety of mixtures. Similarly, the pressure and composition dependence of upper critical solution phenomena can be accurately predicted. Progress has been achieved in predicting discontinuous critical transitions in polar and nonpolar binary mixtures. There is increasing interest in calculating the critical properties of ternary and multicomponent mixtures. Although the techniques applied to binary mixtures often can be directly extended to ternary mixture calculations, calculated critical properties of ternary mixtures indicate that their behavior cannot be considered as a simple extension of binary mixture phenomena. Consequently, ternary critical calculations are likely to provide a superior insight into the phase behavior of multicomponent fluids.
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页码:1376 / 1403
页数:28
相关论文
共 207 条
[1]   A NEW MIXING RULE MODIFIED CONVENTIONAL MIXING RULE [J].
ADACHI, Y ;
SUGIE, H .
FLUID PHASE EQUILIBRIA, 1986, 28 (02) :103-118
[2]   3-PARAMETER EQUATIONS OF STATE [J].
ADACHI, Y ;
LU, BCY ;
SUGIE, H .
FLUID PHASE EQUILIBRIA, 1983, 13 (OCT) :133-142
[3]   STUDIES IN MOLECULAR DYNAMICS .2. BEHAVIOR OF A SMALL NUMBER OF ELASTIC SPHERES [J].
ALDER, BJ ;
WAINWRIGHT, TE .
JOURNAL OF CHEMICAL PHYSICS, 1960, 33 (05) :1439-1451
[4]  
Allen M.P., 1987, COMPUTER SIMULATION
[5]   EQUATION-OF-STATE METHODS FOR THE MODELING OF PHASE-EQUILIBRIA [J].
ANDERKO, A .
FLUID PHASE EQUILIBRIA, 1990, 61 (1-2) :145-225
[6]  
[Anonymous], LIQUIDS LIQUID MIXTU
[7]   CRITICAL-POINT AND SATURATION PRESSURE CALCULATIONS FOR MULTIPOINT SYSTEMS [J].
BAKER, LE ;
LUKS, KD .
SOCIETY OF PETROLEUM ENGINEERS JOURNAL, 1980, 20 (01) :15-24
[8]   THERMODYNAMIC STABILITY-CRITERION FOR PURE SUBSTANCES AND MIXTURES [J].
BEEGLE, BL ;
MODELL, M ;
REID, RC .
AICHE JOURNAL, 1974, 20 (06) :1200-1206
[9]   PERTURBED HARD-CHAIN THEORY - EQUATION OF STATE FOR FLUIDS CONTAINING SMALL OR LARGE MOLECULES [J].
BERET, S ;
PRAUSNITZ, JM .
AICHE JOURNAL, 1975, 21 (06) :1123-1132
[10]   CRITICAL-POINT CALCULATION WITH NONZERO INTERACTION PARAMETERS [J].
BILLINGSLEY, DS ;
LAM, S .
AICHE JOURNAL, 1986, 32 (08) :1393-1396