Phase behavior, densities, and isothermal compressibility of CO2 plus pentane and CO2 plus acetone systems in various phase regions

被引:60
作者
Chen, JW [1 ]
Wu, WZ [1 ]
Han, BX [1 ]
Gao, L [1 ]
Mu, TC [1 ]
Liu, ZM [1 ]
Jiang, T [1 ]
Du, JM [1 ]
机构
[1] Chinese Acad Sci, Inst Chem, Ctr Mol Sci, Beijing 100080, Peoples R China
关键词
D O I
10.1021/je034087q
中图分类号
O414.1 [热力学];
学科分类号
摘要
The phase behavior and critical parameters of CO2 (1) + pentane (2) and CO2 (1) + acetone (2) were determined experimentally, and their densities were measured in both the subcritical and supercritical regions. The isothermal compressibility (K-T) was calculated using the density data. It is demonstrated that the density is sensitive to pressure as the pressure approaches the critical point of the mixtures, that is, K-T is large and increases sharply. K-T also increases significantly as the pressure approaches the dew point or the bubble point at other compositions close to the critical composition. However, K-T is very small and is not sensitive to pressure well above the dew point or the bubble point. When the composition is far from the critical one, K-T is fairly small and the effect of pressure on K-T is very limited, even near the phase separation point.
引用
收藏
页码:1544 / 1548
页数:5
相关论文
共 27 条
[1]   High-pressure multiphase behaviour of ternary systems carbon dioxide water polar solvent: Review and modeling with the Peng-Robinson equation of state [J].
Adrian, T ;
Wendland, M ;
Hasse, H ;
Maurer, G .
JOURNAL OF SUPERCRITICAL FLUIDS, 1998, 12 (03) :185-221
[2]   PHOTO-FRIES REARRANGEMENT OF NAPHTHYL ACETATE IN SUPERCRITICAL CARBON-DIOXIDE - CHEMICAL EVIDENCE FOR SOLVENT-SOLUTE CLUSTERING [J].
ANDREW, D ;
ISLET, BTD ;
MARGARITIS, A ;
WEEDON, AC .
JOURNAL OF THE AMERICAN CHEMICAL SOCIETY, 1995, 117 (22) :6132-6133
[3]  
[Anonymous], 1999, CHEM SYNTHESIS USING
[4]   High-pressure (vapour plus liquid) equilibria in (carbon dioxide plus acetone or 2-propanol) at temperatures from 293 K to 333 K [J].
Bamberger, A ;
Maurer, G .
JOURNAL OF CHEMICAL THERMODYNAMICS, 2000, 32 (05) :685-700
[5]   EQUILIBRIUM-PHASE PROPERTIES OF N-PENTANE-CARBON DIOXIDE SYSTEM [J].
BESSERER, GJ ;
ROBINSON, DB .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1973, 18 (04) :416-419
[6]   VAPOR LIQUID EQUILIBRIUM IN THE SYSTEM CARBON-DIOXIDE + N-PENTANE FROM 252-K TO 458-K AT PRESSURES TO 10-MPA [J].
CHENG, HZ ;
DEFERNANDEZ, MEP ;
ZOLLWEG, JA ;
STREETT, WB .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1989, 34 (03) :319-323
[7]   SOLUTE SOLUTE AND SOLUTE SOLVENT CORRELATIONS IN DILUTE NEAR-CRITICAL TERNARY MIXTURES - MIXED-SOLUTE AND ENTRAINER EFFECTS [J].
CHIALVO, AA .
JOURNAL OF PHYSICAL CHEMISTRY, 1993, 97 (11) :2740-2744
[8]   Polymer synthesis and processing using supercritical carbon dioxide [J].
Cooper, AI .
JOURNAL OF MATERIALS CHEMISTRY, 2000, 10 (02) :207-234
[9]   MODIFICATION OF SUPERCRITICAL FLUID PHASE-BEHAVIOR USING POLAR COSOLVENTS [J].
DOBBS, JM ;
WONG, JM ;
LAHIERE, RJ ;
JOHNSTON, KP .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1987, 26 (01) :56-65
[10]   SOLUTE PARTIAL MOLAL VOLUMES IN SUPERCRITICAL FLUIDS [J].
ECKERT, CA ;
ZIGER, DH ;
JOHNSTON, KP ;
KIM, S .
JOURNAL OF PHYSICAL CHEMISTRY, 1986, 90 (12) :2738-2746