CALCULATION METHOD FOR VAPOR-LIQUID-EQUILIBRIUM IN THE CRITICAL REGION

被引:7
作者
ALSAHHAF, TA [1 ]
SLOAN, ED [1 ]
KIDNAY, AJ [1 ]
机构
[1] COLORADO SCH MINES,DEPT CHEM & PETR REFINING ENGN,GOLDEN,CO 80401
关键词
D O I
10.1002/aic.690300537
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
引用
收藏
页码:867 / 871
页数:5
相关论文
共 13 条
[1]  
ALSAHHAF T, 1982, THESIS COLORADO SCH
[2]   LIQUID-VAPOR EQUILIBRIA AT 250.00K FOR SYSTEMS CONTAINING METHANE, ETHANE, AND CARBON-DIOXIDE [J].
DAVALOS, J ;
ANDERSON, WR ;
PHELPS, RE ;
KIDNAY, AJ .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1976, 21 (01) :81-84
[3]   CRITICAL POINTS IN MULTICOMPONENT SYSTEMS [J].
GRIFFITH.RB ;
WHEELER, JC .
PHYSICAL REVIEW A-GENERAL PHYSICS, 1970, 2 (03) :1047-&
[5]   THERMODYNAMIC PROPERTIES NEAR LIQUID-VAPOR CRITICAL LINE IN MIXTURES OF HE-3 AND HE-4 [J].
LEUNG, SS ;
GRIFFITHS, RB .
PHYSICAL REVIEW A, 1973, 8 (05) :2670-2683
[6]  
Levelt Sengers J.M.H., 1976, J PHYS CHEM REF DATA, V5, P1
[7]   CRITICAL-POINTS OF MIXTURES - ANALOGY WITH PURE FLUIDS [J].
MOLDOVER, MR ;
GALLAGHER, JS .
AICHE JOURNAL, 1978, 24 (02) :267-278
[8]  
Oellrich L, 1981, INT CHEM ENG, V21, P1
[9]   PHASE EQUILIBRIA IN HYDROCARBON SYSTEMS - THE NORMAL-BUTANE-CARBON DIOXIDE SYSTEM [J].
OLDS, RH ;
REAMER, HH ;
SAGE, BH ;
LACEY, WN .
INDUSTRIAL AND ENGINEERING CHEMISTRY, 1949, 41 (03) :475-482
[10]   A New Two-Constant Equation of State [J].
PENG, D ;
ROBINSON, DB .
INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1976, 15 (01) :59-64