Implementation of PC-SAFT and SAFT + Cubic for modeling thermodynamic properties of haloalkanes. II. 7 Haloethanes and their mixtures

International Journal of Refrigeration

Volumn 36, Issue 3, 2013, Pages 980-991

  Polishuk, Ilya ^a   Assor, Erez ^a   Cohen, Naor ^a   Potievsky, Rostislav ^a  

^a ARIEL UNIVERSITY   (Israel)

Author keywords

Density; Fluid; Heat capacity; Phase equilibria; Refrigerants; Sound velocity; Statistics; Theory

Indexed keywords

CONSTANT-PRESSURE CONDITIONS; ENGINEERING EQUIPMENTS; ERROR CANCELLATION; HALOALKANES; ISOBARIC HEAT CAPACITY; PC-SAFT; PURE COMPOUNDS; THEORY;

ACOUSTIC WAVE VELOCITY; DENSITY (SPECIFIC GRAVITY); ESTIMATION; FLUIDS; FORECASTING; PHASE EQUILIBRIA; REFRIGERANTS; STATISTICS;

SPECIFIC HEAT;

EID: 84875219890     PISSN: 01407007     EISSN: None     Source Type: Journal    
DOI: 10.1016/j.ijrefrig.2012.10.034     Document Type: Article

References (44)

1. I. Astina, and H. Sato A fundamental equation of state for 1,1,1,2-tetrafluoroethane with an intermolecular potential energy background and reliable ideal-gas properties Fluid Phase Equilib. 221 2004 103 111
2. R.C. Downing Fluorocarbon Refrigerants Handbook 1988 Prentice Hall Englewood Cliffs, NJ, USA
3. J.M.S.S. Esperanca, P.F. Pires, H.J.R. Guedes, N. Ribeiro, T. Costa, and A. Aguiar-Ricardo Acoustic determination of thermophysical properties and critical parameters for the mixture (51 wt % R143a + 49 wt % R125) and critical line of xCO2 + (1-x) (51 wt % R143a + 49 wt % R125) J. Chem. Eng. Data 51 2006 2161 2169
4. J.M.S.S. Esperanca, P.F. Pires, H.J.R. Guedes, N. Ribeiro, T. Costa, and A. Aguiar-Ricardo Acoustic determination of thermophysical properties and critical parameters for R404A and critical line of xCO2 + (1-x) R404A J. Chem. Eng. Data 51 2006 1148 1155
5. V. Feroiu, and D. Geana Vapor-liquid equilibrium thermodynamic and volumetric properties of refrigerants from cubic equations of state Sci. Technol. Environ. Prot. 9 2002 23 35
6. V. Feroiu, and D. Geana Volumetric and thermodynamic properties for pure refrigerants and refrigerant mixtures from cubic equations of state Fluid Phase Equilib. 207 2003 283 300
7. V. Feroiu, D. Geana, and C. Secuianu Properties of refrigerants from cubic equations of state Rev. Chim. (Bucharest, Rom.) 59 2008 554 557
8. V. Feroiu, and D. Geana Properties of pure refrigerants and refrigerant mixtures from cubic equations of state Rev. Roum. Chim. 56 2011 517 525
9. A.P. Fröba, S. Will, and A. Leipertz Thermophysical properties of binary and ternary fluid mixtures from dynamic light scattering Int. J. Thermophys. 22 2001 1349 1368
10. A.P. Fröba, and A. Leipertz Thermophysical properties of the refrigerant mixtures R410A and R407C from dynamic light scattering (DLS) Int. J. Thermophys. 24 2003 1185 1206
11. A. Galindo, A. Gil-Villegas, P.J. Whitehead, G. Jackson, and A.N. Burgess Prediction of phase equilibria for refrigerant mixtures of difluoromethane (HFC-32), 1,1,1,2-Tetrafluoroethane (HFC-134a) and pentafluoroethane (HFC-125a), using SAFT-VR J. Phys. Chem. A 102 1998 7632 7639
12. J. Gross, and G. Sadowski Perturbed-Chain SAFT: an equation of state based on a perturbation theory for chain molecules Ind. Eng. Chem. Res. 40 2001 1244 1260
13. H.J.R. Guedes, and J.A. Zollweg Speed of sound in liquid R134a Int. J. Refrigeration 15 1992 381 385
14. R. Kato, K. Shirakawa, and H. Nishiumi Critical locus and vapor-liquid equilibria of HFC32-HFC125 system Fluid Phase Equilib. 194-197 2002 995 1008
15. G. Kishizawa, H. Sato, and K. Watanabe Measurements of saturation densities in critical region and critical loci for binary R-32/125 and R-125/143a systems Int. J. Thermophys. 20 1999 923 932
16. E.W. Lemmon, and R.T. Jacobsen An international standard formulation for the thermodynamic properties of 1,1,1-Trifluoroethane (HFC-143a) for Temperatures from 161 to 450 K and pressures to 50 MPa J. Phys. Chem. Ref. Data 29 2000 521 552
17. E.W. Lemmon, and R.T. Jacobsen Equations of state for mixtures of R-32, R-125, R-134a, R-143a and R-152a J. Phys. Chem. Ref. Data 33 2004 593 620
18. E.W. Lemmon, and R.T. Jacobsen A new functional form and new fitting techniques for equations of state with application to pentafluoroethane (HFC-125) J. Phys. Chem. Ref. Data 34 2005 69 108
19. R. Malhotra, and L.A. Woolf An automated volumometer: thermodynamic properties of 1,1-dichloro-2,2,2-trifluoroethane (R123) for temperatures of 278.15 to 338.15 K and pressures of 0.1 to 380 MPa Int. J. Thermophys. 14 1993 1021 1038
20. R. Malhotra, and L.A. Woolf PVT Property Measurements for Liquid 1,2-dichloro-1,2,2-trifluoroethane from 278 to 338 K J. Chem. Eng. Data 41 1996 254 257
21. R. Malhotra, and L.A. Woolf Volumetric measurements for 1,1-dichloro-1-fluoroethane (R141b) in the temperature range 278.15 to 338.15 K and pressure range from 0.1 to 380 MPa Fluid Phase Equilib. 92 1994 195 213
22. C. McCabe, A. Galindo, A. Gil-Villegas, and G. Jackson Predicting the high-pressure phase equilibria of binary mixtures of perfluoro-n-alkanes + n-alkanes using the SAFT-VR approach J. Phys. Chem. A 102 1998 8060 8069
23. M.O. McLinden Thermodynamic properties of CFC [chlorofluorocarbon] alternatives: a survey of the available data Int. J. Refrigeration 13 1990 149 162
24. K. Mejbri, and A. Bellagi PC-SAFT equation of state applied to pure fluids and to binary mixtures J. de la Societe Chimique de Tunisie 7 2005 125 142 http://www.sctunisie.org/pdf/journaux/journal%20n7/volume%201/JSCT-v7-n1-16- 125.pdf
25. Monsalvo, M.A.; 2006. Phase behavior and viscosity modeling of refrigerant-lubricant mixtures, In: Ph D thesis (Eds.), Technical University of Denmark, Lyngby. http://orbit.dtu.dk/fedora/objects/orbit:82741/datastreams/ file-5085416/content.
26. H. Nishiumi, H. Akita, and S. Akiyama High pressure vapor-liquid equilibria for the HFC125-HFC152a system Korean J. Chem. Eng. 14 1997 359 364
27. S.L. Outcalt, and M.O. McLinden A modified Benedict-Webb-Rubin equation of state for the thermodynamic properties of R152a (1,1-difluoroethane) J. Phys. Chem. Ref. Data 25 1996 605 636
28. B.E. Poling, G.H. Thomson, D.G. Friend, R.L. Rowley, and W.V. Wilding Perry's Chemical Engineers' Handbook eighth ed. 2008 McGraw Hill New York
29. I. Polishuk Hybridizing SAFT and cubic EOS: what can Be Achieved? Ind. Eng. Chem. Res. 50 2011 4183 4198
30. I. Polishuk Till which pressures the fluid phase EOS models might stay reliable? J. Supercrit. Fluids 58 2011 204 215
31. I. Polishuk, M. Katz, Y. Levi, and H. Lubarsky Implementation of PC-SAFT and SAFT + Cubic for modeling thermodynamic properties of haloalkanes Fluid Phase Equilib. 316 2012 66 73
32. W. Poot, and T.W. de Loos High pressure phase behavior of binary systems of refrigerants and phenylalkanes: the system 1,1,1,2-tetrafluoroethane + phenyloctane Fluid Phase Equilib. 222-223 2004 255 259
33. S.L. Randzio, E.T. Wilhelm, and M. Letcher Heat Capacities Liquids, Solutions and Vapors 2010 RSC Publishing Cambridge 153-185
34. N. Ribeiro, T. Costa, A. Aguiar-Ricardo, J.M.S.S. Esperanca, P.F. Pires, and H.J.R. Guedes Acoustic determination of thermophysical properties and critical parameters for R410A and critical line of xCO2 + (1-x) R410A J. Chem. Eng. Data 51 2006 1906 1914
35. G. Scalabrin, P. Marchi, and R. Span A reference multiparameter viscosity equation for R134a with an optimized functional J. Phys. Chem. Ref. Data 35 2006 839 868
36. W.F. Stoecker Industrial Refrigeration Handbook 1998 McGraw-Hill
37. S. Swaminathan, and D.;P. Visco Jr. Thermodynamic modeling of refrigerants using the statistical associating fluid theory with variable range. 1. pure components Ind. Eng. Chem. Res. 44 2005 4798 4805
38. S. Swaminathan, and D.;P. Visco Jr. Thermodynamic modeling of refrigerants using the statistical associating fluid theory with variable range. 2. Applications to binary mixtures Ind. Eng. Chem. Res. 44 2005 4806 4814
39. T. Takagi Ultrasonic speed for liquid trichlorofluoromethane and 1,1-dichloro-2,2,2-trifluoroethane at temperatures from 283 to 373 K and pressures up to 75 MPa J. Chem. Eng. Data 36 1991 394 398
40. T. Takagi, M. Kusunoki, and M. Hongo Speed of sound in liquid 1,2-dichloro-1,2,2-trifluoroethane from 283 to 373 K and up to 75 MPa J. Chem. Eng. Data 37 1992 39 41
41. T. Takagi, and M. Hongo Ultrasonic speeds in liquid 1,1-dichloro-1- fluoroethane at temperatures from 283 to 373 K and pressures up to 50 MPa J. Chem. Eng. Data 38 1993 60 62
42. T. Takagi Ultrasonic speed in the liquid phase under high pressures and bubble point pressure for mixtures of HFC-125/HFC-134a High Temp.-High Press. 29 1997 135 141
43. O. Vilaseca, F. Llovell, J. Yustos, R.M. Marcos, and L.F. Vega Phase equilibria, surface tensions and heat capacities of hydrofluorocarbons and their mixtures including the critical region J. Supercrit. Fluids 55 2010 755 768
44. B.A. Younglove, and M.O. McLinden An international standard equation of state for the thermodynamic properties of refrigerant 123 (2,2-dichloro-1,1,1- trifluoroethane) J. Phys. Chem. Ref. Data 23 1994 731 779