VOLUMETRIC AND PHASE BEHAVIOR IN THE ETHANE-PROPENE SYSTEM

被引：59

作者：

MCKAY, RA

REAMER, HH

SAGE, BH

LACEY, WN

机构：

来源：

INDUSTRIAL AND ENGINEERING CHEMISTRY | 1951年 / 43卷 / 09期

关键词：

D O I：

10.1021/ie50501a039

中图分类号：

O69 [应用化学];

学科分类号：

081704 ;

摘要：

引用

页码：2112 / 2117

页数：6

共 24 条

[1]

BARKELEW CH, 1947, CHEM ENG PROG, V43, P25

[2] The compressibility of gaseous ethane in the high density region [J].

Beattie, JA ;

Su, GJ ;

Simard, GL .

JOURNAL OF THE AMERICAN CHEMICAL SOCIETY, 1939, 61 :926-927

[3] A new equation of state for fluids. [J].

Beattie, JA ;

Bridgeman, OC .

PROCEEDINGS OF THE AMERICAN ACADEMY OF ARTS AND SCIENCES, 1928, 63 (1/8) :229-308

[4] The compressibility of and an equation of state for gaseous ethane [J].

Beattie, JA ;

Hadlock, C ;

Poffenberger, N .

JOURNAL OF CHEMICAL PHYSICS, 1935, 3 (02) :93-96

[5]

Benedict M, 1940, J CHEM PHYS, V8, P334, DOI [10.1063/1.1750658, DOI 10.1063/1.1750658]

[6] PHASE BEHAVIOR IN THE METHANE-ETHANE-NORMAL-PENTANE SYSTEM [J].

BILLMAN, GW ;

SAGE, BH ;

LACEY, WN .

TRANSACTIONS OF THE AMERICAN INSTITUTE OF MINING AND METALLURGICAL ENGINEERS, 1948, 174 :13-24

[7] A fixed point for the calibration of pressure gages. The vapor pressure of liquid carbon dioxide at 0 degrees [J].

Bridgeman, OC .

JOURNAL OF THE AMERICAN CHEMICAL SOCIETY, 1927, 49 :1174-1183

[8] VOLUMETRIC BEHAVIOR OF PROPENE [J].

FARRINGTON, PS ;

SAGE, BH .

INDUSTRIAL AND ENGINEERING CHEMISTRY, 1949, 41 (08) :1734-1737

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

Kay, WB .

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

[10]

KUENEN JP, 1906, THEORIE VERDAMPFUNG

← 1 2 3 →