45
Views
0
CrossRef citations to date
0
Altmetric
Original Articles

VAPOR-LIQUID EQUILIBRIUM MEASUREMENT AND DATA TREATMENT OF n-PROPANOL AND ISOBUTANOL MIXTURE AT ATMOSPHERIC PRESSURE

&
Pages 205-224 | Received 11 Oct 1996, Published online: 30 Mar 2007

References

  • Anderson , T. F. and Prausnitz , J. M. ( 1978 ) “ Application of The UNIQUAC Equation to Calculation of Multicomponent Phase Equilibria. I. Vapor Liquid Equilibria ”, Ind. Eng. Chem. Process Des Dev. , 17 , 552 .
  • Anderson , T. F. , Abrams , D. S. and Grens II , E. A. ( 1978 ) “ Evaluation of Parameter for Nonlinear Thermodynamic Models ”, AlChE J. , 24 , 20 .
  • Box , M. J. (1970) “Improved Parameter Estimation”, Technometrics , 12, 219.
  • Britt , H. I. and Luecke , R. H. ( 1973 ) “ The Estimation of Parameters in Nonlinear, Implicit Models ”, Technometrics , 15 , 233 .
  • Byer , S. M. , Gibbs , R. E. and van Ness , H. C. ( 1973 ) “ Vapor-Liquid Equilibrium: Part II. Correlations from P-x Data for 15 Systems ”, AIChE J. , 19 , 245 .
  • Cholinski , J. , Palczewska-Tulinska , M., Szafranska , A. and Wyrzykowskastankiewicz , D. ( 1981 ) “ A New Method of Parameter Adjustment and Diagnostic Checks on Gamma Models Used in Vapor-Liquid Equilibrium Calculations ”, Chemical Engineering Science , 36 , 173 .
  • Dohnal , V. and Fenclova , D. ( 1985 ) “ Verification of The Accuracy of Complete Binary Vapor-Liquid Equilibrium Data ”, Fluid Phase Equilibria. , 19 , 1 .
  • Englezos , P. and Kalogerakis , N. ( 1993 ) “ Constrained Least Squares Estimation of Binary Interaction Parameters in Equations of State ”, Computers Chem. Engng. , 17 , 117 .
  • Englezos , P. , Kalogerakis , N. , Trebble , M. A. and Bishnoi , P. R. ( 1990 ) “ Estimation of Multiple Binary Interaction Parameters in Equations of State Using VLE Data. Application to The Trebble-Bishnoi Equation ”, Fluid Phase Equilibria , 58 , 117 .
  • Englezos , P. , Kalogerakis , N. and Bishnoi , P. R. ( 1993 ) “ A Systematic Approach for the Efficient Estimation of Interaction Parameters in Equations of State Using Binary VLE Data ”, The Canadian Journal of Chemical Engineering , 71 , 322 .
  • Fabries , J. F. and Renon , H. ( 1975 ) “ Method of Evaluation and Reduction of Vapor-Liquid Equilibrium Data of Binary Mixture ”, AIChE J. , 21 , 735 .
  • Gmehling , J. , Onken , U. and Weidlich , U. ( 1977 ) DECHEMA Chemistry Data Ser., , D. Behrens and R. Eckermann , Eds., DECHEMA Publishers , Frankfurt , Germany , 1 , Part 2a, 540 .
  • Hayden , J. G. and O'Connell , J. P. ( 1975 ) “ A Generalized Method for Predicting Second Virial Coefficients ”, Ind. Eng. Chem., Process Des. Dev. , 14 , 209 .
  • Herington ., E. F. G. ( 1965 ) “ Test for The Consistency of Experimental Isobaric Vapor-Liquid Equilibrium ”, J. Inst. Petro. , 37 , 456 .
  • Kemeny , S. and Manczinger , J. ( 1982 ) “ Reduction of Thermodynamic Data by Means of The Multiresponse Maximum Likelihood Principle ”, AIChE J. , 28 , 20 .
  • Kemeny , S. and Manczinger , J. ( 1978 ) “ Treatment of Binary Vapor-Liquid Equilibrium Data ”, Chemical Engineering Science , 33 ,71.
  • Lee , L. S. , Huang , J. F. , Yang , W. Y. and Chiang , A. S. T. ( 1994 ) “ Vapor-Liquid Equilibrium Measurements and Data Analysis of Isoprene and n-Pentane Mixture ”, Fluid Phase Equilibria , 102 , 257 .
  • Linnik , J. W. ( 1961 ) Die Metode der kleinsten Quadrate in moderner Darstellung, VEB Deutsche Verlag der Wissenschaften, , Berlin .
  • Mendenhall , W. ( 1971 ) Introduction to Probability and Statistics, , Third Edition, Duxbury Press Company Inc., Belmont , California .
  • Neau , E. and Peneloux , A. ( 1981 ) “ Estimation of Model Parameters. Comparison of Methods Based on The maximum Likelihood Principle ”, Fluid Phase Equilibria , 6 , 1 .
  • Patino-Leal , H. and Reilly , P. M. ( 1982 ) “ Statistical Estimation of Parameters in Vapor-Liquid Equilibrium ”, AIChE J. , 28 , 580 .
  • Renon , H. and Prausnitz , J. M. ( 1968 ) “ Local Compositions in Thermodynamic Excess Function for Liquid Mixtures ”, AIChE J. , 14 , 135 .
  • Rod , V. and Vladislav , H. ( 1980 ) “ Iterative Estimation of Model Parameters When Measurements of All Variables are Subject to Error ”, Computers and Chemical Engineering , 4 , 33 .
  • Rubio , R. G. , Renuncio , J. A. R. and Pena , M. D. ( 1983 ) “ Regression of Vapor-Liquid Equilibrium Data Based on Application of The Maximum Likelihood Principle ”, Fluid Phase Equilibria , 12 , 217 .
  • Spencer , C. F. and Danner , R. P. ( 1973 ) Improved Equation for Prediction of Saturated Liquid Density , J. Chem. Eng. Data , 18 , 230 .
  • Sutton , T. L. and Macgregor , J. F. ( 1977 ) “ The Analysis and Design of Binary Vapor-Liquid Equilibrium Experiments, Part I: Parameter Estimation and Consistency Test ”, The Canadian Journal of Chemical Engineering , 55 , 602 .
  • Van Ness , H. C. , Byer , S. M. and Gibbs , R. E. ( 1973 ) “ Vapor-Liquid Equilibrium Part I. An Appraisal of Data Reduction Method ”, AlChE J. , 19 , 238 .
  • Wilson , G. M. ( 1964 ) “ Vapor-Liquid Equilibrium. XI. A New Expression for The Excess Free Energy of Mixing ”, J. Am. Chem. Soc. , 86 , 127 .
  • Wisniak , J. ( 1993 ) “ Pitfalls in Fitting Binary Vapor-Liquid Equilibria Data with Two Parameter Equations ”, Fluid Phase Equilibria , 89 , 291 .
  • Corresponding author.

Reprints and Corporate Permissions

Please note: Selecting permissions does not provide access to the full text of the article, please see our help page How do I view content?

To request a reprint or corporate permissions for this article, please click on the relevant link below:

Academic Permissions

Please note: Selecting permissions does not provide access to the full text of the article, please see our help page How do I view content?

Obtain permissions instantly via Rightslink by clicking on the button below:

If you are unable to obtain permissions via Rightslink, please complete and submit this Permissions form. For more information, please visit our Permissions help page.