Ten serwis zostanie wyłączony 2025-02-11.
Nowa wersja platformy, zawierająca wyłącznie zasoby pełnotekstowe, jest już dostępna.
Przejdź na https://bibliotekanauki.pl

PL EN


Preferencje help
Widoczny [Schowaj] Abstrakt
Liczba wyników
Czasopismo
2014 | 12 | 9 | 918-927
Tytuł artykułu

High-pressure phase equilibrium calculations for carbon dioxide + cyclopentane binary system

Treść / Zawartość
Warianty tytułu
Języki publikacji
EN
Abstrakty
EN
The phase behavior of the carbon dioxide + cycloalkane mixtures usually receives low attention, though these systems are important for many industries, e.g. the carbon capture and storage. In this paper calculations results for the carbon dioxide + cyclopentane binary system are presented, based on SRK and PR cubic equations of state with classical van der Waals mixing rules. A single set of binary parameters for each model was proposed to predict the global phase behavior of the system in a wide range of pressure and temperature. Albeit the thermodynamic models used are simple, they are able to represent fairly well the phase behavior of the system analyzed in this paper.
Słowa kluczowe
Wydawca

Czasopismo
Rocznik
Tom
12
Numer
9
Strony
918-927
Opis fizyczny
Daty
wydano
2014-09-01
online
2014-05-01
Twórcy
autor
  • University Politehnica of Bucharest, S1
  • National University of Córdoba
Bibliografia
  • [1] B. Metz, O. Davidson, H. de Connick, M. Loos, L. Meyer (Eds.), IPCC Special Report on Carbon Dioxide Capture and Storage (Cambridge University Press, Cambridge, New York, Melbourne, Madrid, Cape Town, Singapore, and Sào Paulo, 2005)
  • [2] E.J. Anthony, P.S. Fennell, In: I. Galarraga, M. Gonzalez-Eguino, A. Markandya (Eds.), Handbook of Sustainable Energy (Edward Elgar, Cheltenham, UK and Northampton, MA, USA, 2011) 357
  • [3] E. Hendriks, G.M. Kontogeorgis, R. Dohrn, J.-C. de Hemptinne, I.G. Economou, L. Fele Zilnik, V. Vesovic, Ind. Eng. Chem. Res 49, 11131 (2010) http://dx.doi.org/10.1021/ie101231b[Crossref]
  • [4] M Cismondi, S.B. Rodriguez-Reartes, J.M. Milanesio, M.S. Zabaloy, Ind. Eng. Chem. Res 51, 6232 (2012) http://dx.doi.org/10.1021/ie2018806[Crossref]
  • [5] R. Dohrn, G. Brunner, Fluid Phase Equilib 106, 213 (1995) http://dx.doi.org/10.1016/0378-3812(95)02703-H[Crossref]
  • [6] M. Christov, R. Dohrn, Fluid Phase Equilib 202, 153 (2002) http://dx.doi.org/10.1016/S0378-3812(02)00096-1[Crossref]
  • [7] R. Dohrn, S. Peper, J.M.S. Fonseca, Fluid Phase Equilib 288, 1 (2010) http://dx.doi.org/10.1016/j.fluid.2009.08.008[Crossref]
  • [8] J.M.S. Fonseca, R. Dohrn, S. Peper, Fluid Phase Equilib 300, 1 (2011) http://dx.doi.org/10.1016/j.fluid.2010.09.017[Crossref]
  • [9] DETHERM Database, DECHEMA Chemistry Data Series, Frankfurt, Germany
  • [10] ThermoLit, The National Institute of Standards and Technology (NIST) Literature Report Builder for Thermophysical and Thermochemical Property Measurements (http://trc.nist.gov/thermolit)
  • [11] S. Vitu, R. Privat, J.-N. Jaubert, J. Supercrit. Fluids 45, 1 (2008) http://dx.doi.org/10.1016/j.supflu.2007.11.015[Crossref]
  • [12] J.-N. Jaubert, L. Coniglio, F. Denet, Ind. Eng. Chem. Res 38, 3162 (1999) http://dx.doi.org/10.1021/ie980783l[Crossref]
  • [13] J.-N. Jaubert, L. Coniglio, Ind. Eng. Chem. Res 38, 5011 (1999) http://dx.doi.org/10.1021/ie990544d[Crossref]
  • [14] J.-N. Jaubert, F. Mutelet, Fluid Phase Equilib 224, 285 (2004) http://dx.doi.org/10.1016/j.fluid.2004.06.059[Crossref]
  • [15] J.-N. Jaubert, S. Vitu, F. Mutelet, J.-P. Corriou, Fluid Phase Equilib 237, 193 (2005) http://dx.doi.org/10.1016/j.fluid.2005.09.003[Crossref]
  • [16] S. Vitu, J.-N. Jaubert, F. Mutelet, Fluid Phase Equilib 243, 9 (2006) http://dx.doi.org/10.1016/j.fluid.2006.02.004[Crossref]
  • [17] S. Vitu, R. Privat, J.N. Jaubert, F. Mutelet, J. Supercrit. Fluid 45, 1 (2008) http://dx.doi.org/10.1016/j.supflu.2007.11.015[Crossref]
  • [18] R. Privat, J.-N. Jaubert, F. Mutelet, Ind. Eng. Chem. Res 47, 2033 (2008) http://dx.doi.org/10.1021/ie071524b[Crossref]
  • [19] R. Privat, F. Mutelet, J.-N. Jaubert, Ind. Eng. Chem. Res 47, 10041 (2008) http://dx.doi.org/10.1021/ie800799z[Crossref]
  • [20] R. Privat, J.-N. Jaubert, F. Mutelet, J. Chem. Thermodyn 40, 1331 (2008) http://dx.doi.org/10.1016/j.jct.2008.05.013[Crossref]
  • [21] R. Privat, J.-N. Jaubert, F. Mutelet, Ind. Eng. Chem. Res 47, 7483 (2008) http://dx.doi.org/10.1021/ie800636h[Crossref]
  • [22] J.-N. Jaubert, R. Privat, F. Mutelet, AIChE J 56, 3225 (2010) http://dx.doi.org/10.1002/aic.12232[Crossref]
  • [23] R. Privat, J.-N. Jaubert, Fluid Phase Equilib 334, 197 (2012) http://dx.doi.org/10.1016/j.fluid.2012.08.007[Crossref]
  • [24] J.-W. Qian, J.-N. Jaubert, R. Privat, J. Supercrit. Fluid 75, 58 (2013) http://dx.doi.org/10.1016/j.supflu.2012.12.014[Crossref]
  • [25] J.-W. Qian, J.-N. Jaubert, R. Privat, Fluid Phase Equilib 354, 212 (2013) http://dx.doi.org/10.1016/j.fluid.2013.06.040[Crossref]
  • [26] J.-W. Qian, R. Privat, J.-N. Jaubert, P. Duchet-Suchaux, Energ. Fuel 27, 7150 (2013) http://dx.doi.org/10.1021/ef401605c[Crossref]
  • [27] J.-W. Qian, R. Privat, J.-N. Jaubert, Ind. Eng. Chem. Res. doi: 10.1021/ie402541h (2013) [Crossref]
  • [28] D.-Y. Peng, D.B. Robinson, Ind. Eng. Chem. Fundam 15, 59 (1976) http://dx.doi.org/10.1021/i160057a011[Crossref]
  • [29] G. Soave, Chem. Eng. Sci 27, 1197 (1972) http://dx.doi.org/10.1016/0009-2509(72)80096-4[Crossref]
  • [30] M. Nakajima, R. Ohmura, Y.H. Mori, Ind. Eng. Chem. Res 47, 8933 (2008) http://dx.doi.org/10.1021/ie800949k[Crossref]
  • [31] K. Freeman, GE Appliances, 28 Apr 2011, 1
  • [32] Y. Ishida, Y. Takahashi, R. Ohmura, Cryst. Growth Des 12, 3271 (2012) http://dx.doi.org/10.1021/cg300416x[Crossref]
  • [33] C.J. Eckert, S.I. Sandler, J. Chem. Eng. Data 31, 26 (1983) http://dx.doi.org/10.1021/je00043a008[Crossref]
  • [34] P. Marathe, S.I. Sandler, J. Chem. Eng. Data 36, 192 (1991) http://dx.doi.org/10.1021/je00002a015[Crossref]
  • [35] N.N. Shah, J.A. Zollweg, W.B. Streett, J. Chem. Eng. Data 36, 188 (1991) http://dx.doi.org/10.1021/je00002a014[Crossref]
  • [36] R. Privat, J.-N. Jaubert, Chem. Eng. Res. Des 91, 1807 (2013) http://dx.doi.org/10.1016/j.cherd.2013.06.026[Crossref]
  • [37] P.H. van Konynenburg, R.L. Scott, Philos. Trans. R. Soc. London, Ser. A 298, 495 (1980) http://dx.doi.org/10.1098/rsta.1980.0266[Crossref]
  • [38] C. Secuianu, V. Feroiu, D. Geană, J. Chem. Eng. Data 54, 1493 (2009) http://dx.doi.org/10.1021/je800799n[Crossref]
  • [39] C. Secuianu, V. Feroiu, D. Geană, J. Supercritical Fluids 55, 653 (2010) http://dx.doi.org/10.1016/j.supflu.2010.09.018[Crossref]
  • [40] C. Secuianu, V. Feroiu, D. Geană, J. Chem. Thermodyn 42, 1286 (2010) http://dx.doi.org/10.1016/j.jct.2010.05.006[Crossref]
  • [41] C. Secuianu, V. Feroiu, D. Geană, Intern. J. Liq. State Sci 2, 1 (2010)
  • [42] C. Secuianu, V. Feroiu, D. Geană, J. Chem. Eng. Data 55, 4255 (2010) http://dx.doi.org/10.1021/je100404g[Crossref]
  • [43] C. Secuianu, V. Feroiu, D. Geană, J. Chem. Eng. Data 56, 5000 (2011) http://dx.doi.org/10.1021/je200867n[Crossref]
  • [44] C. Secuianu, J. Qian, R. Privat, J.-N. Jaubert, Ind. Eng. Chem. Res 51, 11284 (2012) http://dx.doi.org/10.1021/ie3015186[Crossref]
  • [45] J.A.P. Coutinho, G. M. Kontogeorgis, E.H. Stenby, Fluid Phase Equilib 102, 31 (1994) http://dx.doi.org/10.1016/0378-3812(94)87090-X[Crossref]
  • [46] Y.S. Wei, R.J. Sadus, AIChE J 46, 169 (2000) http://dx.doi.org/10.1002/aic.690460119[Crossref]
  • [47] J.O. Valderrama, Ind. Eng. Chem. Res 42, 1603 (2003) http://dx.doi.org/10.1021/ie020447b[Crossref]
  • [48] S. Vitu, J.-N. Jaubert, J. Pauly, J.-L. Daridon, J. Chem. Thermodyn 40, 1358 (2008) http://dx.doi.org/10.1016/j.jct.2008.05.008[Crossref]
  • [49] S. Vitu, J.-N. Jaubert, J. Pauly, J.-L. Daridon, D. Barth, J. Supercrit. Fluids 44, 155 (2008) http://dx.doi.org/10.1016/j.supflu.2007.10.003[Crossref]
  • [50] D. Geană, L. Rus, In Proceedings of 14th Romanian International Conference on Chemistry and Chemical Engineering, 4–7 Sep 2005, Bucharest, Romania 170
  • [51] M. Cismondi, M. Gaitan, GPEC Global Phase Equilibrium Calculations (National University of Cordoba, Cordoba, 2012)
  • [52] Evaluated Standard Thermophysical Property Values, DIPPR Project 801 full version (Department of Chemistry and Engineering, Brigham Young University, Provo, Utah, 2005)
  • [53] R. Privat, PhD Thesis (Nancy University, Nancy, France, 2008) (in French)
Typ dokumentu
Bibliografia
Identyfikatory
Identyfikator YADDA
bwmeta1.element.-psjd-doi-10_2478_s11532-013-0393-2
JavaScript jest wyłączony w Twojej przeglądarce internetowej. Włącz go, a następnie odśwież stronę, aby móc w pełni z niej korzystać.