VAPOR-LIQUID-EQUILIBRIA IN ALKAN-1-OL PLUS N-ALKANE MIXTURES

被引:10
作者
DYMOND, JH
机构
[1] Department of Chemistry, University of Glasgow
关键词
D O I
10.1351/pac199466030553
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
Recommended values are given for vapour-liquid equilibria. excess molar enthalpies, excess molar he-at capacities. liquid-liquid equilibria, excess molar volumes, activity coefficients at infinite dilution and solid-liquid equilibria for binary alkan-1-ol + n-alkane mixtures. In addition, recommended values are reported for certain properties of the pure components: volumetric properties of gases, orthobaric liquid densities, compressibilities, critical properties, heat capacities, vapour pressures and enthalpies of vaporization.
引用
收藏
页码:553 / 564
页数:12
相关论文
共 42 条
[1]   VAPOR-PRESSURES UP TO THEIR CRITICAL-TEMPERATURES OF NORMAL ALKANES AND 1-ALKANOLS [J].
AMBROSE, D ;
WALTON, J .
PURE AND APPLIED CHEMISTRY, 1989, 61 (08) :1395-1403
[2]  
AMBROSE D, 1978, 92 NAT PHYS LAB REP
[3]  
[Anonymous], 1993, METHANOL INT THERMOD
[4]  
[Anonymous], 1985, IUPAC CHEM DATA SER
[5]   CORRELATION OF LLE IN 1-ALKANOL+N-ALKANE BINARY-MIXTURES USING THE MODIFIED WILSON EQUATION [J].
ARAI, Y ;
HIGASHIUCHI, H ;
SAKURAGI, Y .
FLUID PHASE EQUILIBRIA, 1993, 89 (01) :187-196
[6]   THERMODYNAMICS OF 1-ALKANOL+N-ALKANE MIXTURES BASED ON PREDICTIONS OF THE ERAS MODEL [J].
BENDER, M ;
HEINTZ, A .
FLUID PHASE EQUILIBRIA, 1993, 89 (01) :197-215
[7]   SATURATED LIQUID DENSITIES OF 1-ALKANOLS FROM C(1) TO C(10) AND N-ALKANES FROM C(5) TO C(16) - A CRITICAL-EVALUATION OF EXPERIMENTAL-DATA [J].
CIBULKA, I .
FLUID PHASE EQUILIBRIA, 1993, 89 (01) :1-18
[8]   DEVELOPMENT OF A VAPOR-PRESSURE EQUATION FOR METHANOL [J].
CRAVEN, RJB ;
DEREUCK, KM .
FLUID PHASE EQUILIBRIA, 1993, 89 (01) :19-29
[9]   AN EQUATION OF STATE FOR THE GAS-PHASE OF METHANOL [J].
CRAVEN, RJB ;
DEREUCK, KM ;
WAKEHAM, WA .
PURE AND APPLIED CHEMISTRY, 1989, 61 (08) :1379-1386
[10]   A NEW SEMI-EMPIRICAL EQUATION OF STATE FOR FLUIDS .2. APPLICATION TO PURE SUBSTANCES [J].
DEITERS, U .
CHEMICAL ENGINEERING SCIENCE, 1981, 36 (07) :1147-1151