HIGH-PRESSURE VAPOR LIQUID EQUILIBRIA INVOLVING MIXTURES OF NITROGEN, CARBON-DIOXIDE, AND N-BUTANE

被引：69

作者：

SHIBATA, SK ^{[1
]}

SANDLER, SI ^{[1
]}

机构：

[1] UNIV DELAWARE,DEPT CHEM ENGN,NEWARK,DE 19716

来源：

JOURNAL OF CHEMICAL AND ENGINEERING DATA | 1989年 / 34卷 / 03期

关键词：

D O I：

10.1021/je00057a011

中图分类号：

O414.1 [热力学];

学科分类号：

摘要：

引用

页码：291 / 298

页数：8

共 7 条

[1] VOLUMETRIC AND PHASE BEHAVIOR OF NITROGEN-HYDROCARBON SYSTEMS - NITROGEN-BUTANE SYSTEM [J].

AKERS, WW ;

ATTWELL, LL ;

ROBINSON, JA .

INDUSTRIAL AND ENGINEERING CHEMISTRY, 1954, 46 (12) :2539-2540

[2] VAPOR-LIQUID-EQUILIBRIA FOR THE CARBON DIOXIDE-1-BUTENE SYSTEM AT 37.7-DEGREES-C AND 45.0-DEGREES-C [J].

BEHRENS, PK ;

SANDLER, SI .

JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1983, 28 (01) :52-56

[3] VAPOR-LIQUID-EQUILIBRIA FOR THE CARBON-DIOXIDE CYCLOPENTANE SYSTEM AT 37.7-DEGREES-C, 45.0-DEGREES-C, AND 60.0-DEGREES-C [J].

ECKERT, CJ ;

SANDLER, SI .

JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1986, 31 (01) :26-28

[4]

Knapp H., 1982, DECHEMA CHEM DATA SE, V6

[5] PHASE EQUILIBRIA IN HYDROCARBON SYSTEMS - THE NORMAL-BUTANE-CARBON DIOXIDE SYSTEM [J].

OLDS, RH ;

REAMER, HH ;

SAGE, BH ;

LACEY, WN .

INDUSTRIAL AND ENGINEERING CHEMISTRY, 1949, 41 (03) :475-482

[6] A New Two-Constant Equation of State [J].

PENG, D ;

ROBINSON, DB .

INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1976, 15 (01) :59-64

[7] VAPOR-LIQUID EQUILIBRIUM IN THE NORMAL-BUTANE-NITROGEN SYSTEM [J].

ROBERTS, LR ;

MCKETTA, JJ .

AICHE JOURNAL, 1961, 7 (01) :173-174

← 1 →