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LIQUID-LIQUID-VAPOR EQUILIBRIA IN NITROGEN-METHANE-ETHANE SYSTEM
被引:33
作者
:
YU, P
论文数:
0
引用数:
0
h-index:
0
机构:
Department of Chemical Engineering, University of Ottawa, Ottawa, Ontario
YU, P
ELSHAYAL, IM
论文数:
0
引用数:
0
h-index:
0
机构:
Department of Chemical Engineering, University of Ottawa, Ottawa, Ontario
ELSHAYAL, IM
LU, BCY
论文数:
0
引用数:
0
h-index:
0
机构:
Department of Chemical Engineering, University of Ottawa, Ottawa, Ontario
LU, BCY
机构
:
[1]
Department of Chemical Engineering, University of Ottawa, Ottawa, Ontario
来源
:
CANADIAN JOURNAL OF CHEMICAL ENGINEERING
|
1969年
/ 47卷
/ 05期
关键词
:
D O I
:
10.1002/cjce.5450470516
中图分类号
:
TQ [化学工业];
学科分类号
:
0817 ;
摘要
:
Liquid‐liquid‐vapor equilibrium compositions were measured for the nitrogen‐ethane binary and the nitrogen‐methane‐ethane ternary systems from –255° to –219.8°F and at pressures up to 591 psia. A forced‐recirculation apparatus was employed for the determinations. Experimental results were interpreted and correlated. Optimum operating temperature for nitrogen separation has been suggested. Copyright © 1969 Canadian Society for Chemical Engineering
引用
收藏
页码:495 / &
相关论文
共 5 条
[1]
Chang S. -D., 1967, CHEM ENG PROG S SER, V63, P18
[2]
Din F, 1962, THERMODYNAMIC FUNCTI
[3]
EAKIN BE, 1955, 26 I GAS TECHN RES B
[4]
Ellington R., 1959, THERMODYNAMIC TRANSP, P180
[5]
TREYBAL RE, 1951, LIQUID EXTRACTION, P22
←
1
→
共 5 条
[1]
Chang S. -D., 1967, CHEM ENG PROG S SER, V63, P18
[2]
Din F, 1962, THERMODYNAMIC FUNCTI
[3]
EAKIN BE, 1955, 26 I GAS TECHN RES B
[4]
Ellington R., 1959, THERMODYNAMIC TRANSP, P180
[5]
TREYBAL RE, 1951, LIQUID EXTRACTION, P22
←
1
→