Measurement of bubble point pressures and critical points of carbon dioxide and chlorodifluoromethane mixtures using the variable-volume view cell apparatus

2000 ◽  
Vol 17 (5) ◽  
pp. 510-515 ◽  
Author(s):  
Jae Min Lee ◽  
Byung-Chul Lee ◽  
Chan-Hwi Cho
Keyword(s):  
Carbon Dioxide ◽  
Critical Points ◽  
Bubble Point ◽  
Variable Volume

Dew and bubble point measurements for carbon dioxide-propane mixtures

1984 ◽  
Vol 29 (3) ◽  
pp. 304-309 ◽  
Author(s):  
Julio C. Acosta ◽  
Edison Hevia ◽  
Stuart Leipziger
Keyword(s):  
Carbon Dioxide ◽  
Bubble Point

Bubble Point Simulation of Reservoir Oil and Carbon Dioxide Mixtures

2016 ◽  
Vol 42 (4) ◽  
pp. 1633-1641 ◽  
Author(s):  
Rashid S. Mohammad ◽  
Xinzhe Zhao ◽  
Shicheng Zhang ◽  
Syed Jamal-ud-Din Shah
Keyword(s):  
Carbon Dioxide ◽  
Bubble Point

Bubble-point measurements in the ammonia-carbon dioxide system

2007 ◽  
Vol 21 (8) ◽  
pp. 229-232 ◽  
Author(s):  
S. M. Lemkowitz ◽  
J. Goedegebuur ◽  
P. J. Berg
Keyword(s):  
Carbon Dioxide ◽  
Bubble Point

scholarly journals Phase equilibria experiments and calculations for carbon dioxide + methanol binary system

2009 ◽  
Vol 7 (1) ◽  
pp. 1-7 ◽  
Author(s):  
Catinca Secuianu ◽  
Viorel Feroiu ◽  
Dan Geană
Keyword(s):  
Carbon Dioxide ◽  
Phase Behavior ◽  
Analytic Method ◽  
Visual Cell ◽  
Uniquac Model ◽  
Variable Volume ◽  
Vle Data ◽  
Vapor Liquid Equilibria ◽  
Methanol System ◽  
Made In

AbstractVapor-liquid equilibria (VLE) data for the carbon dioxide + methanol system was measured at 293.15, 298.15, 310.15, and 323.15 K. Phase behavior measurements were made in a high-pressure visual cell with variable volume, based on the static-analytic method. The pressure range under investigation was between 4.8 and 95.1 bar. The Soave-Redlich-Kwong (SRK)-EOS coupled with Huron-Vidal (HV) mixing rules and a reduced UNIQUAC model, was used in a semi-predictive approach, in order to represent the phase behavior (critical curve, isothermal VLE) of the system. The topology of the phase behavior of the carbon dioxide + methanol system is satisfactory predicted with the SRK/HV-residual UNIQUAC model.

Bubble point measurements for the ternary system carbon dioxide, benzene and naphthalene

1990 ◽  
Vol 55 (1-2) ◽  
pp. 231-240 ◽  
Author(s):  
Taher A. Al-Sahhaf ◽  
Rasheed S. Al-Ameeri ◽  
Inas M. Nashef ◽  
Salah E.M. Hamam
Keyword(s):  
Carbon Dioxide ◽  
Ternary System ◽  
Bubble Point
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