ISOTHERMAL VAPOR-LIQUID-EQUILIBRIA FOR METHANOL PLUS ETHANOL PLUS WATER, METHANOL PLUS WATER, AND ETHANOL PLUS WATER

被引：112

作者：

KURIHARA, K

MINOURA, T

TAKEDA, K

KOJIMA, K

机构：

[1] NIHON UNIV, DEPT IND CHEM, CHIYODA KU, TOKYO 101, JAPAN

[2] MITUI ENGN & SHIPBLDG CO LTD, TOKYO, JAPAN

来源：

JOURNAL OF CHEMICAL AND ENGINEERING DATA | 1995年 / 40卷 / 03期

关键词：

D O I：

10.1021/je00019a033

中图分类号：

O414.1 [热力学];

学科分类号：

摘要：

Isothermal vapor-liquid equilibria were measured for the ternary system methanol + ethanol + water and its constituent binary systems of methanol + water and ethanol + water at 323.15, 328.15, and 333.15 K. The apparatus that was used made it possible to control the measured temperature and total pressure by computer. The experimental binary data were correlated by the NRTL equation. The ternary system was predicted using the binary NRTL parameters with good accuracy.

引用

页码：679 / 684

页数：6

共 28 条

[1]

[Anonymous], 1985, PHASE EQUILIBRIA CHE, DOI 10.1016/C2013-0-04304-6

[2] EXCESS THERMODYNAMIC FUNCTIONS FOR TERNARY-SYSTEMS .5. TOTAL-PRESSURE DATA AND GE FOR 1,4-DIOXANE-ETHANOL-WATER AT 50-DEGREES-C [J].