Critical Properties for Carbon Dioxide +n-Alkane Mixtures Using a Variable-Volume View Cell

1998 ◽  
Vol 43 (5) ◽  
pp. 714-716 ◽  
Author(s):  
Eun-Joo Choi ◽  
Sang-Do Yeo
1998 ◽  
Vol 43 (4) ◽  
pp. 683-686 ◽  
Author(s):  
J. Todd Reaves ◽  
Aron T. Griffith ◽  
Christopher B. Roberts

2018 ◽  
Vol 240 ◽  
pp. 01036
Author(s):  
Marcin Wołowicz ◽  
Jarosław Milewski ◽  
Piotr Lis

The paper aims to compare the models of working fluids against experimental data for carbon dioxide close to its critical conditions. Fortunately, most of the work is already done and published where the authors compared the models based on the equation of the state (EoS). There are a few other models which were not investigated, thus we would like to add a few new results here and focus only on near-critical properties where the biggest deviation between experimental and calculated properties can be observed. The area of interest was pressure range of 7.39 – 20 MPa and temperature range of 304-340 K just above fluid critical point (7.39 MPa, 304.25 K). Model validation was performed for density and heat capacity as one of the most important parameters in preliminary cycle analysis.


2009 ◽  
Vol 113 (20) ◽  
pp. 7243-7256 ◽  
Author(s):  
Sofía T. Blanco ◽  
Laura Gil ◽  
Pilar García-Giménez ◽  
Manuela Artal ◽  
Santos Otín ◽  
...  

2006 ◽  
Vol 248 (2) ◽  
pp. 191-196 ◽  
Author(s):  
Delin Qiu ◽  
Jinyan Fu ◽  
Jun Cai ◽  
Changjun Peng ◽  
Honglai Liu ◽  
...  

2009 ◽  
Vol 7 (1) ◽  
pp. 1-7 ◽  
Author(s):  
Catinca Secuianu ◽  
Viorel Feroiu ◽  
Dan Geană

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.


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