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Application of the mathematical models of distillation equilibria for designing the differential distillation process

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Warianty tytułu
Języki publikacji
EN
Abstrakty
EN
This paper presents the development of mathematical models for positive and negative azeotropes in the range of the more volatile concentrations component: x∈[0; az] ∨ [az; 1]. The coefficients of these models, which, on their basis, were determined the relative volatility of α and the azeotrope concentration az, defined with the high accuracy (R2∈[0,926; 0,999]) and presented them to the table for all subjects of distillation systems. Based on these relationships, the integration of the mass balance equations of the distillation differential process d(Sx)=ydS was carried out and determined the dependence of the distillate obtained from 1 mole of pig iron D/S0 from the α, az coefficients and xw, xs concentrations. Based on these dependencies, charts D/S0 were prepared from predefined by the authors parameter t=[0,05; 0,25; 0,5; 0,75] which is the change in the concentration of pig iron in the process of concentration. Dependencies, presented for distillation balances of positive and negative azeotrope, in the tested ranges, for similar values of α, have the same mileage. The calculations were made for the 126 distillation systems.
Rocznik
Tom
Strony
103--116
Opis fizyczny
Bibliogr. 33 poz., rys., tab.
Twórcy
autor
  • Department of Technology and Apparatus of Chemical and Food Industry Faculty of Technology and Chemical Engineering University of Technology and Life Sciences Seminaryjna 3, 85-326 Bydgoszcz, Poland
autor
  • Department of Technology and Apparatus of Chemical and Food Industry Faculty of Technology and Chemical Engineering University of Technology and Life Sciences Seminaryjna 3, 85-326 Bydgoszcz, Poland
autor
  • Faculty of Civil Engineering Cracow University of Technology Warszawska 24, 31-155 Cracow, Poland
Bibliografia
  • [1] Orchilles A. V., Miguel P. J., Vercher E., Martínez-Andreu A., 2007. Ionic Liquids as Entrainers in Extractive Distillation: Isobaric Vapor-Liquid Equilibria for Acetone + Methanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate. J. Chem. Eng. Data 52, 141-147.
  • [2] Arce A., Rodil E., Soto A., 2000. Experimental Determination of the Vapor-Liquid Equilibrium at 101.32 kPa of the Ternary System 1-Butanol + Methanol + TAME. J. Chem. Eng. Data 45, 1112-1115.
  • [3] Pereiro A.B., Rodríguez A., Canosa J., Tojo J., 2005. Measurement of the Isobaric Vapor-Liquid Equilibria of Dimethyl Carbonate with Acetone, 2-Butanone, and 2-Pentanone at 101.3 kPa and Density and Speed of Sound at 298.15 K. J. Chem. Eng. Data 50, 481-486.
  • [4] Gomez-Marigliano A. C., Arce A., Rodil E., Soto A., 2010. Isobaric Vapor-Liquid Equilibria at 101.32 kPa and Densities, Speeds of Sound, and Refractive Indices at 298.15 K for MTBE or DIPE or TAME + 1-Propanol Binary Systems. J. Chem. Eng. Data 55, 92-97.
  • [5] Dejoz A., González-Alfaro V., Llopis F.J., Miguel P.J., Vázquez M.I., 1999. Vapor-Liquid Equilibrium of Binary Mixtures of Tetrachloroethylene with 1-Pentanol, 3-Methyl-1-butanol, and 2-Methyl-1-butanol. J. Chem. Eng. Data 44, 286-290.
  • [6] Mejia A., Segura H., Cartes M., 2010. Vapor-Liquid Equilibria and Interfacial Tensions of the System Ethanol + 2-Methoxy-2-methylpropane. J. Chem. Eng. Data 55, 428-434.
  • [7] Aucejo A., Gabaldón C., Loras S., Marzal P., Sanchotello M., 2003. Phase Equilibria in the Binary and Ternary Systems Composed of Diethyl Ketone, 2-Pentanone, and 3-Pentanol at 101.3 kPa. J. Chem. Eng. Data 48, 1128-1131.
  • [8] Aucejo A., Loras S., Muñoz R., Wisniak J., Segura H., 1997. Phase Equilibria and Multiple Azeotropy in the Associating System Methanol + Diethylamine. J. Chem. Eng. Data 42, 1201-1207.
  • [9] Atik Z., 2007. Experimental Isobaric Vapor-Liquid Equilibria of Binary Mixtures of 2,2,2-Trifluoroethanol with Benzene or Toluene. J. Chem. Eng. Data 52, 1086-1088.
  • [10] Gill B. K., Rattan V. K., Kapoor S., 2008. Experimental Isobaric Vapor-Liquid Equilibrium Data for Binary Mixtures of Cyclic Ethers with (1-Methylethyl)benzene. J. Chem. Eng. Data 53, 2041-2043.
  • [11] Gill B. K., Rattan V. K., Kapoor S., 2009. Vapor-Liquid Equilibrium Data for N-Methylacetamide and N,N-Dimethylacetamide with Cumene at 97.3 kPa. J. Chem. Eng. Data 54, 1175-1178.
  • [12] Bandrowski, J., Palica, M. 2005. Materiały pomocnicze co ćwiczeń i projektów z inżynierii chemicznej. Gliwice: Wydawnictwo Politechniki Śląskiej.
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  • [15] Vercher E., Rojo F.J., Martínez-Andreu A., 1999. Isobaric Vapor-Liquid Equilibria for 1-Propanol + Water + Calcium Nitrate. J. Chem. Eng. Data 44, 1216-1221.
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  • [17] Monick J.A., Allen H.D., Marlies C.J., 1946. Vapor-Liquid Equilibrium Data for Fatty Acids and Fatty Methyl Esters at Low Pressures. Journal of the American Oil Chemists' Society 23(6), 177-182.
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  • [19] Cai J., Cui X., Zhang Y., Li R., Feng T., 2011. Vapor-Liquid Equilibrium and Liquid-Liquid Equilibrium of Methyl Acetate + Methanol + 1-Ethyl-3-methylimidazolium Acetate. J. Chem. Eng. Data 56(2), 282-287.
  • [20] Korea Thermophysical Properties Data Bank. Pobrano Styczeń 12, 2011 z lokalizacji Chemical Engineering Research Information Center: http://www.cheric.org/research/kdb/hcvle/hcvle.php
  • [21] Vijayaraghavan S.V., Deshpande P.K., Kuloor N.R., 1967. Vapor-liquid Equilibrium Data for the Systems Diisopropyl Ether-n-Heptane and Diisopropyl Ether-Carbon Tetrachloride at Medium Pressures 12(1), 15-17.
  • [22] Thiede S., Horstmann S., Gmehling J., 2010. Vapor-Liquid Equilibrium Data, Excess Enthalpy Data, and Azeotropic Data for the Binary System Dibutyl Ether + o-Xylene. J. Chem. Eng. Data 55, 3155-3159.
  • [23] Kapoor S., Gill B.K., Rattan V.K., 2008. Isobaric Vapor-Liquid Equilibrium of Binary Mixture of Methyl Acetate with Isopropylbenzene at 97.3 kPa. World Academy of Science, Engineering and Technology 47, 37-40.
  • [24] Serwiński M., 1965. Tabele liczbowe z Inżynierii Chemicznej. Politechnika Łódzka.
  • [25] Serwiński M., 1982. Zasady inżynierii chemicznej i procesowej. WNT Warszawa.
  • [26] Sobczak E.R., 2010. Matematyczny model równowagi destylacyjnej i jego zastosowanie do projektowania procesów destylacji i rektyfikacji. Inżynieria i aparatura chemiczna 49(41), 99-100.
  • [27] Loras S., Aucejo A., Montón J.B., Wisniak J., Segura H., (2002). Phase Equilibria for 1,1,1,2,3,4,4,5,5,5-Decafluoropentane + 2-Methylfuran, 2-Methylfuran + Oxolane, and 1,1,1,2,3,4,4,5,5,5-Decafluoropentane + 2-Methylfuran + Oxolane at 35 kPa. J. Chem. Eng. Data 47, 1256-1262.
  • [28] Troniewski L. (red.), (2006). Tablice do obliczeń procesowych. Politechnika Opolska.
  • [29] Rattan V.K., Gill B.K., Kapoor S., 2008. Isobaric Vapor-Liquid Equilibrium Data for Binary Mixture of 2-Methyltetrahydrofuran and Cumene. World Academy of Science, Engineering and Technology 47, 41-44.
  • [30] Martınez-Soria V., Peña M. P., Montón J.B., 1999. Vapor-Liquid Equilibria for the Binary Systems Isobutyl Alcohol + Toluene, + Isooctane, and + Methylcyclohexane at 101.3 kPa. J. Chem. Eng. Data 44, 608-612.
  • [31] Vijayaraghavan V., Deshpande P.K., Kuloor N.R., 1967. Vapor-liquid Equilibrium Data for the System n-Heptane-n-Butyl Alcohol at Medium Pressures. J. Chem. Eng. Data 12(1), 13-15.
  • [32] Cui W., Zhu J., Liu W., Wu B., Chen K., (2008). Isobaric Vapor–Liquid Equilibria for Binary Systems of Acetone + Isopropenyl Acetate, 2-Butanone + Isopropenyl Acetate, and Isopropenyl Acetate + Acetylacetone at 101.3 kPa. J. Chem. Eng. Data 53, 503-507.
  • [33] Zhang X., Zuo J., Jian Ch., 2010. Experimental Isobaric Vapor-Liquid Equilibrium for Binary Systems of Ethyl Methyl Carbonate + Methanol, + Ethanol, + Dimethyl Carbonate, or + Diethyl Carbonate at 101.3 kPa. J. Chem. Eng. Data 55, 4896-4902.
Typ dokumentu
Bibliografia
Identyfikator YADDA
bwmeta1.element.baztech-08a758f1-f065-4963-89cb-3db81d97b539
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