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2014 | 12 | 9 | 953-961
Tytuł artykułu

New high-pressures vapor-liquid equilibrium data for the carbon dioxide + 2-methyl-1-propanol (isobutanol) binary system

Treść / Zawartość
Warianty tytułu
Języki publikacji
EN
Abstrakty
EN
New vapor-liquid equilibria (VLE) data at 333.15, 343.15, and 353.15 K and pressures up to 130.0 bar are reported for the carbon dioxide + 2-methyl-1-propanol (isobutanol) system. The experimental method used in this work was a static analytical method with liquid and vapor phases sampling using a rapid online sampler injector (ROLSITM) coupled to a gas chromatograph (GC) for analysis. Measured VLE data and literature data for carbon dioxide + 2-methyl-1-propanol system were modeled with the Soave-Redlich-Kwong (SRK) cubic equation of state with classical van der Waals (two-parameter conventional mixing rule, 2PCMR) mixing rules. A single set of interaction parameters that lead to a correct phase behavior was used in this work to model the new VLE data and critical points of the mixtures in a wide range of temperature and pressure. The SRK prediction results were compared to the new data measured in this study and to available literature data.
Wydawca

Czasopismo
Rocznik
Tom
12
Numer
9
Strony
953-961
Opis fizyczny
Daty
wydano
2014-09-01
online
2014-05-01
Twórcy
autor
  • University Politehnica of Bucharest
autor
  • University Politehnica of Bucharest
Bibliografia
  • [1] 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]
  • [2] R. Dohrn, G. Brunner, Fluid Phase Equilib 106, 213 (1995) http://dx.doi.org/10.1016/0378-3812(95)02703-H[Crossref]
  • [3] M. Christov, R. Dohrn, Fluid Phase Equilib 202, 153 (2002) http://dx.doi.org/10.1016/S0378-3812(02)00096-1[Crossref]
  • [4] 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]
  • [5] 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]
  • [6] N. Juntarachat, S. Bello, R. Privat, J.-N. Jaubert, J. Chem. Eng. Data 58, 671 (2013) http://dx.doi.org/10.1021/je301209u[Crossref]
  • [7] R. Privat, J.-W. Qian, D. Alonso, J.-N. Jaubert, Energy 55, 594 (2013) http://dx.doi.org/10.1016/j.energy.2013.03.081[Crossref]
  • [8] J.-N. Jaubert, R. Privat, F. Mutelet, AIChE J 56, 3225 (2010) http://dx.doi.org/10.1002/aic.12232[Crossref]
  • [9] J.-N. Jaubert, L. Coniglio, F. Denet, Ind. Eng. Chem. Res 38, 3162 (1999) http://dx.doi.org/10.1021/ie980783l[Crossref]
  • [10] J.-N. Jaubert, L. Coniglio, Ind. Eng. Chem. Res 38, 5011 (1999) http://dx.doi.org/10.1021/ie990544d[Crossref]
  • [11] S. Sima, V. Feroiu, D. Geană, Fluid Phase Equilib 325, 45 (2012) http://dx.doi.org/10.1016/j.fluid.2012.03.028[Crossref]
  • [12] C. Secuianu, J. Qian, R. Privat, J.-N. Jaubert, Ind. Eng. Chem. Res 51, 11284 (2012) http://dx.doi.org/10.1021/ie3015186[Crossref]
  • [13] C. Secuianu, V. Feroiu, D. Geană, J. Chem. Eng. Data 56, 5000 (2011) http://dx.doi.org/10.1021/je200867n[Crossref]
  • [14] S. Sima, V. Feroiu, D. Geană, J. Chem. Eng. Data 56, 5052 (2011) http://dx.doi.org/10.1021/je2008186[Crossref]
  • [15] C. Secuianu, V. Feroiu, D. Geană, J. Supercrit. Fluid 55, 653 (2010) http://dx.doi.org/10.1016/j.supflu.2010.09.018[Crossref]
  • [16] C. Secuianu, V. Feroiu, D. Geană, J. Chem. Thermodyn 42, 1286 (2010) http://dx.doi.org/10.1016/j.jct.2010.05.006[Crossref]
  • [17] C. Secuianu, V. Feroiu, D. Geană, Rev. Chim. (Bucharest) 60, 472 (2009)
  • [18] C. Secuianu, V. Feroiu, D. Geană, J. Chem. Eng. Data 54, 1493 (2009) http://dx.doi.org/10.1021/je800799n[Crossref]
  • [19] C. Secuianu, V. Feroiu, D. Geană, Cent. Eur. J. Chem 7, 1 (2009) http://dx.doi.org/10.2478/s11532-008-0085-5[Crossref]
  • [20] C. Secuianu, V. Feroiu, D. Geană, J. Supercrit. Fluid 47, 109 (2008) http://dx.doi.org/10.1016/j.supflu.2008.08.004[Crossref]
  • [21] C. Secuianu, V. Feroiu, D. Geană, J. Chem. Eng. Data 53, 2444 (2008) http://dx.doi.org/10.1021/je8004485[Crossref]
  • [22] C. Secuianu, V. Feroiu, D. Geană, Fluid Phase Equilib 270, 109 (2008) http://dx.doi.org/10.1016/j.fluid.2008.06.020[Crossref]
  • [23] C. Secuianu, V. Feroiu, D. Geană, Rev. Chim. (Bucharest) 58, 1176 (2007)
  • [24] C. Secuianu, V. Feroiu, D. Geană, Fluid. Phase Equilib 261, 337 (2007) http://dx.doi.org/10.1016/j.fluid.2007.07.001[Crossref]
  • [25] C. Secuianu, V. Feroiu, D. Geană, J. Chem. Eng. Data 49, 1635 (2004) http://dx.doi.org/10.1021/je0499521[Crossref]
  • [26] C. Secuianu, V. Feroiu, D. Geană, U.P.B. Sci. Bull. Series B 66, 9 (2004)
  • [27] C. Secuianu, V. Feroiu, D. Geană, J. Chem. Eng. Data 48, 1384 (2003) http://dx.doi.org/10.1021/je034027k[Crossref]
  • [28] C. Secuianu, V. Feroiu, D. Geană, Rev. Chim. (Bucuresti) 54, 874 (2003)
  • [29] T. Benali, D. Tondeur, J.-N Jaubert, Appl. Therm. Eng 40, 132 (2012) http://dx.doi.org/10.1016/j.applthermaleng.2012.02.004[Crossref]
  • [30] A. Staby, J. Mollerup, Fluid Phase Equilib 89, 351 (1993) http://dx.doi.org/10.1016/0378-3812(93)85094-3[Crossref]
  • [31] C. Secuianu, V. Feroiu, D. Geană, Ann. W.U.T. Series Chemistry, 12, 393 (2003)
  • [32] C. Secuianu, V. Feroiu, D. Geană, Int. J. Liq. State Sci 2, 1 (2010)
  • [33] S. Ioniţă, V. Feroiu, D. Geană, J. Chem. Eng. Data (in press) doi: 10.1021/je4005239 (2013) [Crossref]
  • [34] S. Sima, C. Secuianu, V. Feroiu, D. Geană, New high-pressures vapor-liquid equilibrium data for the carbon dioxide + 2-methyl-2-propanol binary system, Cent. Eur. J. Chem. (2013) (in press)
  • [35] DETHERM Database (DECHEMA Chemistry Data Series, Frankfurt, Germany, 1991–2010)
  • [36] ThermoLit, Literature Report Builder for Thermophysical and Thermochemical Property Measurements (The National Institute of Standards and Technology (NIST), Boulder, Colorado, USA, 2012) (http://trc.nist.gov/thermolit)
  • [37] A.I. Semenova, E.A. Emelyanova, S.S. Tsimmerman, D.S. Tsiklis, Russ. J. Phys. Chem 52, 655 (1978)
  • [38] Z. Yun, M. Shi, J. Shi, J. Fuel Chem. Technol 24, 87 (1996)
  • [39] N. Zhang, X. Zheng, Nat. Gas Chem. Ind 24, 54 (1997)
  • [40] M. V. da Silva, D. Barbosa, Fluid Phase Equilib 198, 229 (2002) http://dx.doi.org/10.1016/S0378-3812(01)00766-X[Crossref]
  • [41] H.-I. Chen, P.-H. Chen, H.-Y. Chang, J. Chem. Eng. Data 48, 1407 (2003) http://dx.doi.org/10.1021/je020214r[Crossref]
  • [42] I. Gainar, D. Bala, An. Univ. Bucuresti Chim 13, 213 (2004)
  • [43] H. Inomata, A. Kondo, H. Kakehashi, Fluid Phase Equilib 228–229, 335 (2005) http://dx.doi.org/10.1016/j.fluid.2004.09.033[Crossref]
  • [44] L. Wang, R.L. Li, L.T. Sun, K.X. Chen, Chem. J. Chinese U 30, 1631 (2009)
  • [45] J.E. Gutierrez, A. Bejarano, J.C. de la Fuente, J. Chem. Thermodyn 42, 591 (2010) http://dx.doi.org/10.1016/j.jct.2009.11.015[Crossref]
  • [46] 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]
  • [47] R. Privat, J.-N. Jaubert, Chem. Eng. Res. Des 91, 1807 (2013) http://dx.doi.org/10.1016/j.cherd.2013.06.026[Crossref]
  • [48] E.H. Buechner, Z. Phys. Chem. Stoechiom. Verwandtschaftsl 54, 665 (1906)
  • [49] Th.W. de Loos, in: E. Kiran, J.M.H. Levelt Sengers (Eds.), Supercritical Fluids: Fundamentals for Applications (Kluwer Academic Publishers, Dordrecht, 1994) 65 http://dx.doi.org/10.1007/978-94-015-8295-7_3[Crossref]
  • [50] G. Soave, Chem. Eng. Sci 27, 1197 (1972) http://dx.doi.org/10.1016/0009-2509(72)80096-4[Crossref]
  • [51] P. Guilbot, A. Valtz, H. Legendre, D. Richon, Analusis 28, 426 (2000) http://dx.doi.org/10.1051/analusis:2000128[Crossref]
  • [52] A. Scheidgen, Ph.D. Thesis (Ruhr-Universität Bochum, Bochum, Germany, 1997)
  • [53] L.A. Galicia-Luna, A. Ortega-Rodriguez, J. Chem. Eng. Data 45, 265 (2000) http://dx.doi.org/10.1021/je990187d[Crossref]
  • [54] D. Geană, L. Rus, In Proceedings of 14th Romanian International Conference on Chemistry and Chemical Engineering, 4–7 Sep 2005, Bucharest, Romania 170
  • [55] M. Cismondi, M. Gaitan, GPEC Global Phase Equilibrium Calculations (National University of Cordoba, Cordoba, 2012) http://gpec.phasety.com
  • [56] Evaluated Standard Thermophysical Property Values, DIPPR Project 801 full version (Department of Chemistry and Engineering, Brigham Young University, Provo Utah, 2005)
Typ dokumentu
Bibliografia
Identyfikatory
Identyfikator YADDA
bwmeta1.element.-psjd-doi-10_2478_s11532-013-0394-1
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