PHASE-EQUILIBRIA IN THE BINARY-SYSTEM CARBON-DISULFIDE CARBON-DIOXIDE

被引：12

作者：

REIFF, WE ^{[1
]}

ROTH, H ^{[1
]}

LUCAS, K ^{[1
]}

机构：

[1] UNIV DUISBERG,FACHGEBIET THERMODYNAM,FACHBEREICH THERMODYNAM 7,LOTHARSTR 1-21,W-4100 DUISBURG 1,GERMANY

来源：

FLUID PHASE EQUILIBRIA | 1992年 / 73卷 / 03期

关键词：

D O I：

10.1016/0378-3812(92)80016-3

中图分类号：

O414.1 [热力学];

学科分类号：

摘要：

Vapor-liquid and three-phase equilibrium compositions for the binary system carbon disulfide-carbon dioxide have been measured at eleven temperatures ranging from 273.15 to 473.15 K At subcritical temperatures the pressure at each temperature ranged from the vapor pressure of carbon disulfide to the vapor pressure of carbon dioxide. Above the critical temperature of carbon dioxide the pressures were extended to the vicinity of the critical region at about 16 MPa. The data were used to investigate the correlative capability of two empirical equations of state as well as the predictive capability of a molecular model based on perturbation theory.

引用

页码：323 / 338

页数：16

共 6 条

[1]

DEITERS UK, 1979, THESIS RUHR U BOCHUM

[2]

LUCAS K, 1991, APPLIED STATISTICAL

[3] A STATIC EQUILIBRIUM APPARATUS FOR (VAPOR + LIQUID) EQUILIBRIUM MEASUREMENTS AT HIGH-TEMPERATURES AND PRESSURES - RESULTS FOR (METHANE + N-PENTANE) [J].