EQUILIBRIUM PHASE PROPERTIES OF TOLUENE-CARBON DIOXIDE SYSTEM

被引：193

作者：

NG, HJ ^{[1
]}

ROBINSON, DB ^{[1
]}

机构：

[1] UNIV ALBERTA,DEPT CHEM ENGN,EDMONTON T6G 2G6,ALBERTA,CANADA

来源：

JOURNAL OF CHEMICAL AND ENGINEERING DATA | 1978年 / 23卷 / 04期

关键词：

D O I：

10.1021/je60079a020

中图分类号：

O414.1 [热力学];

学科分类号：

摘要：

Vapor and liquid equilibrium phase compositions have been determined for the toluene-carbon dioxide binary system at 100.6, 175.0, 249.0, 399.0 ΔF over a pressure range from the vapor pressure of toluene to the critical pressure. The data were used to calculate equilibrium ratios for toluene and carbon dioxide in the binary system. © 1978, American Chemical Society. All rights reserved.

引用

页码：325 / 327

页数：3

共 4 条

[1] APPARATUS FOR ACCURATE DETERMINATIONS OF VAPOR-LIQUID EQUILIBRIUM PROPERTIES AND GAS PVT PROPERTIES
FREDENSLUND, A
MOLLERUP, J
CHRISTIANSEN, LJ
[J]. CRYOGENICS, 1973, 13 (07) : 414 - 419
[2] EQUILIBRIUM PHASE PROPERTIES OF CARBON DIOXIDE NORMAL-HEPTANE SYSTEM
KALRA, H
KUBOTA, H
ROBINSON, DB
NG, HJ
[J]. JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1978, 23 (04) : 317 - 321
[3] APPARATUS FOR SIMULTANEOUS MEASUREMENT OF EQUILIBRIUM PHASE COMPOSITION AND REFRACTIVE-INDEX DATA AT LOW-TEMPERATURES AND HIGH-PRESSURES
KALRA, H
ROBINSON, DB
[J]. CRYOGENICS, 1975, 15 (07) : 409 - 412
[4] A New Two-Constant Equation of State
PENG, D
ROBINSON, DB
[J]. INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1976, 15 (01): : 59 - 64

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