Isothermal vapour-liquid equilibria and excess molar volumes in the binary ethanol plus methyl propanoate or methyl butanoate systems

被引:30
作者
Constantinescu, D [1 ]
Wichterle, I [1 ]
机构
[1] Acad Sci Czech Republ, Inst Chem Proc Fundamentals, E Hala Lab Thermodynam, Prague 16502 6, Czech Republic
关键词
experiment; vapour pressure; low-pressure vapour-liquid equilibrium; azeotropy; excess molar volume; methyl alkanoate; ethanol;
D O I
10.1016/S0378-3812(02)00173-5
中图分类号
O414.1 [热力学];
学科分类号
摘要
Vapour-liquid equilibrium (VLE) data for the binary systems ethanol + methyl propanoate and ethanol + methyl butanoate at 326.30 and 346.30 K and vapour pressures (VPs) for both esters were measured by a circulation method. The two systems exhibit azeotropic behaviour. The VLE data were correlated using the Redlich-Kister, Wilson and NRTL equations. Molar excess volumes for the binary systems at 298.15 K were determined and correlated. (C) 2002 Elsevier Science B.V. All rights reserved.
引用
收藏
页码:71 / 82
页数:12
相关论文
共 18 条
[1]  
AIM K, 1981, 181 ICPF
[2]  
[Anonymous], 1970, TECHNIQUES CHEM
[3]  
Boublik T., 1973, VAPOUR PRESSURES PUR
[4]   LIQUID-VAPOUR EQUILIBRIA .29. MEASUREMENT OF EQUILIBRIUM DATA IN SYSTEMS WITH HIGH EQUILIBRIUM RATIO OF COMPONENTS [J].
DVORAK, K ;
BOUBLIK, T .
COLLECTION OF CZECHOSLOVAK CHEMICAL COMMUNICATIONS, 1963, 28 (05) :1249-&
[5]  
GMEHLING J, 1994, AZEOTROPIC DATA, V1
[6]  
HALA E, 1982, VAPOR LIQUID EQUILIB
[7]   GENERALIZED METHOD FOR PREDICTING 2ND VIRIAL-COEFFICIENTS [J].
HAYDEN, JG ;
OCONNELL, JP .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1975, 14 (03) :209-216
[8]  
HOUGEN OA, 1947, CHEM PROCESS PRINC 2
[9]  
LINEK J, 1995, INT ELECT J PHYS CHE, V1, P23
[10]   ISOBARIC VAPOR-LIQUID-EQUILIBRIUM OF METHYL BUTANOATE WITH ETHANOL AND 1-PROPANOL BINARY-SYSTEMS [J].
ORTEGA, J ;
SUSJAL, P ;
DEALFONSO, C .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1990, 35 (02) :216-219