VAPOR-LIQUID-EQUILIBRIUM DATA AT 1 ATM PRESSURE FOR THE SYSTEMS N-HEPTANE-ISOBUTYL ACETATE, TOLUENE-ISOBUTYL ACETATE AND TOLUENE-N-BUTYL ACETATE

被引:0
作者
MATO, F
BONILLA, D
BENITO, GG
机构
来源
ANALES DE QUIMICA | 1991年 / 87卷 / 05期
关键词
D O I
暂无
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
Vapor-liquid equilibrium data at 1 atm pressure for the systems n-Heptane-Isobutyl Acetate, Toluene-Isobutyl Acetate and Toluene-n-Butyl Acetate are reported. The data were well correlated by different thermodynamic equations. The behaviour of the systems Toluene-Isobutyl Acetate and Toluene-n. Butyl Acetate is close to the ideality.
引用
收藏
页码:660 / 663
页数:4
相关论文
共 13 条
[1]   GENERALIZED METHOD FOR PREDICTING 2ND VIRIAL-COEFFICIENTS [J].
HAYDEN, JG ;
OCONNELL, JP .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1975, 14 (03) :209-216
[2]  
Herington E. F. G., 1951, J I PETROL, V37, P457
[3]   2-PARAMETER MODEL FOR CORRELATING LIQUID-PHASE ACTIVITY-COEFFICIENTS OF BINARY-SYSTEMS [J].
MATO, F ;
MATO, FA .
FLUID PHASE EQUILIBRIA, 1985, 20 (MAR) :183-188
[4]  
MATO F, 1984, AN QUIM A-FIS TEC, V80, P338
[5]  
MATO F, 1985, AN QUIM A-FIS TEC, V81, P400
[6]  
MATO F, 1990, QUIM IND, V36, P543
[7]  
MATO F, 1990, QUIMICA IND, V36, P444
[8]  
Prausnitz J.M., 1967, COMPUTER CALCULATION
[9]   LOCAL COMPOSITIONS IN THERMODYNAMIC EXCESS FUNCTIONS FOR LIQUID MIXTURES [J].
RENON, H ;
PRAUSNITZ, JM .
AICHE JOURNAL, 1968, 14 (01) :135-+
[10]  
Riddick JA., 1986, PHYS PROPERTIES METH