Phase equilibria in hydrocarbon systems - Propane-n-pentane system

被引：102

作者：

Sage, BH ^{[1
]}

Lacey, WN ^{[1
]}

机构：

[1] CALTECH, Pasadena, CA USA

来源：

INDUSTRIAL AND ENGINEERING CHEMISTRY | 1940年 / 32卷

关键词：

D O I：

10.1021/ie50367a030

中图分类号：

O69 [应用化学];

学科分类号：

081704 ;

摘要：

引用

页码：992 / 996

页数：5

共 11 条

[1]

BEATTIE, 1935, J CHEM PHYS, V3, P96

[2] The compressibility of and an equation of state for gaseous propane [J].

Beattie, JA ;

Kay, WC ;

Kaminsky, J .

JOURNAL OF THE AMERICAN CHEMICAL SOCIETY, 1937, 59 :1589-1590

[3] Liquid-vapor phase equilibrium relations in ethane-n-heptane system [J].

Kay, WB .

INDUSTRIAL AND ENGINEERING CHEMISTRY, 1938, 30 :459-465

[4] The osmotic pressure of concentrated solutions, and the laws of the perfect solution. [J].

Lewis, GN .

JOURNAL OF THE AMERICAN CHEMICAL SOCIETY, 1908, 30 (05) :668-683

[5] Phase equilibria in hydrocarbon systems - The propane-n-butane system in the critical region [J].

Nysewander, CN ;

Sage, BH ;

Lacey, WN .

INDUSTRIAL AND ENGINEERING CHEMISTRY, 1940, 32 :118-123

[6]

ROSEINNES, 1899, PHILOS MAG, V47, P353

[7]

SAGE, 1936, IND ENG CHEM, V28, P489

[8] Phase equilibria in hydrocarbon systems VI Thermodynamic properties of normal pentane [J].

Sage, BH ;

Lacey, WN ;

Schaafsma, JG .

INDUSTRIAL AND ENGINEERING CHEMISTRY, 1935, 27 :48-50

[9] Phase equilibria in hydrocarbon systems V Pressure-volume-temperature relations and thermal properties of propane [J].

Sage, BH ;

Schaafsma, JG ;

Lacey, WN .

INDUSTRIAL AND ENGINEERING CHEMISTRY, 1934, 26 :1218-1224

[10]

Taylor H.S., 1939, OIL GAS J, V38, P46

← 1 2 →