Influence of interfacial tension and viscosity on the behavior of a packed column in near-critical fluid extraction

被引:9
作者
Blaha-Schnabel, A [1 ]
Beyer, A [1 ]
Czech, B [1 ]
Jakob, H [1 ]
Schiemann, H [1 ]
Weidner, E [1 ]
Peter, S [1 ]
机构
[1] Univ Erlangen Nurnberg, Inst Chem Tech, D-91058 Erlangen, Germany
关键词
density of fluids; viscosity of fluids; high-pressure interfacial tension; film instability; near-critical extraction;
D O I
10.1080/00986449608936479
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Density and viscosity of the coexisting phases and interfacial tension of the following binary systems were measured: pelargonic acid, linoleic acid, oleic acid or stearic acid as subcritical and carbon dioxide as superecritical components. Also the corresponding phase equilibria were investigated at pressures ranging from 2 to 20 MPa and temperatures from 313 K to 393 K. With increasing pressure the concentration of the supercritical component in the liquid phase increases and viscosity and liquid interfacial tension decreases. At greater activities of the dense gases the interfacial tension decreases dramatically to values less than 2 mN/m if the pressure exceeds a certain limit, a falling film disintegrates into small droplets. The surface excess passes through a maximum at these conditions. At first appearance of instabilities on a falling film, the logarithm of the Reynolds number is a linear function of the logarithm of the film number. Independent of the type of the investigated packings, the number of theoretical stages per meter versus Bodenstein number fall all on the same curve when an extraction is carried out in the droplet regime. Also the logarithm of the capacity of a column at the flooding point versus the logarithm of the density difference between the coexisting phases is a linear function when an extraction is carried out in the droplet regime.
引用
收藏
页码:13 / 31
页数:19
相关论文
共 12 条
[1]  
BLAHASCHNABEL, 1992, THESIS ERLANGEN
[2]  
CZECH B, 1990, HDB 2 INT S HIGH PRE, V1, P419
[3]  
CZECH B, 1991, THESIS ERLANGEN B
[4]  
GRAEF M, 1966, 36 MITT M PLANCK I
[5]  
Hiller N., 1993, CHEM ENG TECHNOL, V16, P206
[6]   GENERALIZED REFERENCE FUGACITIES FOR PHASE EQUILIBRIUM THERMODYNAMICS [J].
LYCKMAN, EW ;
ECKERT, CA ;
PRAUSNIT.JM .
CHEMICAL ENGINEERING SCIENCE, 1965, 20 (07) :685-&
[7]   FRACTIONATION OF GLYCERIDES BY LOW-PRESSURE GAS EXTRACTION [J].
PETER, S ;
WEIDNER, E ;
CZECH, B ;
ENDER, U .
FETT WISSENSCHAFT TECHNOLOGIE-FAT SCIENCE TECHNOLOGY, 1993, 95 :475-482
[8]  
PETER S, 1988, P 1 INT C SUP FLUID, V1, P99
[9]  
PETER S, 1991, SUPERCRITICAL FLUIDS, V4, P116
[10]   EVALUATION OF PACKED-COLUMNS IN SUPERCRITICAL EXTRACTION PROCESSES [J].
RATHKAMP, PJ ;
BRAVO, JL ;
FAIR, JR .
SOLVENT EXTRACTION AND ION EXCHANGE, 1987, 5 (03) :367-391