Solid–liquid equilibrium in ternary mixtures of ethyl oleate, ethyl laurate and ethyl palmitate

2013 ◽  
Vol 339 ◽  
pp. 58-66 ◽  
Author(s):  
Maria Dolores Robustillo ◽  
Deise Fernanda Barbosa ◽  
Antonio José de Almeida Meirelles ◽  
Pedro de Alcântara Pessôa Filho
2013 ◽  
Vol 358 ◽  
pp. 272-281 ◽  
Author(s):  
Maria Dolores Robustillo ◽  
Deise Fernanda Barbosa ◽  
Antonio José de Almeida Meirelles ◽  
Pedro de Alcântara Pessôa Filho

2014 ◽  
Vol 361 ◽  
pp. 188-199 ◽  
Author(s):  
Maria Dolores Robustillo ◽  
Deise Fernanda Barbosa ◽  
Antonio José de Almeida Meirelles ◽  
Pedro de Alcântara Pessôa Filho

2014 ◽  
Vol 370 ◽  
pp. 85-94 ◽  
Author(s):  
Maria Dolores Robustillo ◽  
Deise Fernanda Barbosa ◽  
Antonio José de Almeida Meirelles ◽  
Pedro de Alcântara Pessôa Filho

2021 ◽  
Vol 530 ◽  
pp. 112874
Author(s):  
María Dolores Robustillo ◽  
Larissa Castello Branco Almeida Bessa ◽  
Pedro de Alcântara Pessôa Filho

2016 ◽  
Vol 426 ◽  
pp. 83-94 ◽  
Author(s):  
Maria Dolores Robustillo ◽  
Duclerc Fernandes Parra ◽  
Antonio José de Almeida Meirelles ◽  
Pedro de Alcântara Pessôa Filho

2008 ◽  
Vol 59 (5) ◽  
Author(s):  
Viorel Feroiu ◽  
Dan Geana ◽  
Catinca Secuianu

Vapour � liquid equilibrium, thermodynamic and volumetric properties were predicted for three pure hydrofluorocarbons: difluoromethane (R32), pentafluoroethane (R125) and 1,1,1,2 � tetrafluoroethane (R134a) as well as for binary and ternary mixtures of these refrigerants. Three cubic equations of state GEOS3C, SRK (Soave � Redlich � Kwong) and PR (Peng � Robinson) were used. A wide comparison with literature experimental data was made. For the refrigerant mixtures, classical van der Waals mixing rules without interaction parameters were used. The GEOS3C equation, with three parameters estimated by matching several points on the saturation curve (vapor pressure and corresponding liquid volumes), compares favorably to other equations in literature, being simple enough for applications.


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