Dew points of ternary methane plus ethane plus butane and quaternary methane plus ethane plus butane plus water mixtures:: measurement and correlation

被引：19

作者：

Blanco, ST

Avila, S

Velasco, I

Rauzy, E

Otín, S

机构：

[1] Univ Zaragoza, Fac Ciencia, Dept Quim Organ & Quim Fis, Zaragoza 50009, Spain

[2] Univ Mediterranee, Fac Sci Luminy, Lab Chim Phys Marseille, F-13288 Marseille 9, France

来源：

FLUID PHASE EQUILIBRIA | 2000年 / 171卷 / 1-2期

关键词：

dew point; experimental method; equation of state; excess function;

D O I：

10.1016/S0378-3812(00)00368-X

中图分类号：

O414.1 [热力学];

学科分类号：

摘要：

Dew points for ternary methane + ethane + butane and quaternary methane + ethane + butane + water mixtures were determined experimentally between 4.77 X 10(5) and 99.45 X 10(5) Pa and at temperatures from 250.92 to 288.54 K. The experimental dew point curves of the mixtures with water were reproduced quite accurately with an excess function-equation of state method, independent of the temperature-and pressure ranges. (C) 2000 Elsevier Science B.V. All rights reserved.

引用

页码：233 / 242

页数：10

共 8 条

[1] Water dew points of binary nitrogen plus water and propane plus water mixtures.: Measurement and correlation
Blanco, ST
Velasco, I
Rauzy, E
Otín, S
[J]. FLUID PHASE EQUILIBRIA, 1999, 161 (01) : 107 - 117
[2] HOCQ H, 1994, THESIS U DROIT
[3] EXCESS FUNCTIONS AND EQUATIONS OF STATE
PENELOUX, A
ABDOUL, W
RAUZY, E
[J]. FLUID PHASE EQUILIBRIA, 1989, 47 (2-3) : 115 - 132
[4] A New Two-Constant Equation of State
PENG, D
ROBINSON, DB
[J]. INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1976, 15 (01): : 59 - 64
[5] RAUZY E, 1982, THESIS U AIX MARSEIL
[6] PHASE EQUILIBRIA IN HYDROCARBON SYSTEMS - NORMAL-BUTANE WATER SYSTEM IN THE 2-PHASE REGION
REAMER, HH
SAGE, BH
LACEY, WN
[J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1952, 44 (03): : 609 - 615
[7] Composition of dew-point gas in ethane-water system
Reamer, HH
Olds, RH
Sage, BH
Lacey, WN
[J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1943, 35 : 790 - 793
[8] 1993, 10101 ISO

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