Dossier: Design of Sustainable Processes
Open Access
Oil Gas Sci. Technol. – Rev. IFP Energies nouvelles
Volume 65, Number 5, September-October 2010
Dossier: Design of Sustainable Processes
Page(s) 735 - 749
Published online 22 September 2010
  • Agreda V., Partin L., Heise W. (1990) High-purity Methyl acetate via reactive distillation, Chem. Eng. Prog. 86, 2, 40-46.
  • Barbosa D., Doherty M.F. (1987a) Theory of phase diagrams and azeotropic conditions for two-phase reactive systems, Proc. R. Soc. Lond. A 413, 1845, 443-458. [CrossRef]
  • Barbosa D., Doherty M.F. (1987b) A new set of composition variables for the representation of reactive phase diagrams, Proc. R. Soc. Lond. A 413, 1845, 459-464. [CrossRef]
  • Chakravaty T., Phukan U.K., Weiland R.H. (1985) Reaction of acid gases with mixtures of amines, Chem. Eng. Prog. 81, April, 32-36.
  • Danckwerts P.V. (1951) Continuous flow systems. Distribution of residence times, Chem. Eng. Sci. 2, 1-13.
  • DeCoursey W.J. (1982) Enhancement factors for gas absorption with reversible reaction, Chem. Eng. Sci. 37, 10, 1483-1489. [CrossRef]
  • Doherty M.F. (1990) Topological theory of phase diagrams for reacting mixtures, Proc. R. Soc. Lond. A 430, 1880, 669-678. [CrossRef]
  • Doherty M.F., Huss R.S., Chen F., Malone M.F. (2003) Reactive distillation for methyl acetate production, Comput. Chem. Eng. 27, 12, 1855-1866. [NASA ADS] [CrossRef] [EDP Sciences] [MathSciNet] [PubMed]
  • Doherty M.F., Song W., Venimadhavan G., Manning J.M., Malone M.F. (1998) Measurement of residue curves maps and heterogeneous kinetics in methyl acetate synthesis, Ind. Eng. Chem. Res. 37, 5Dossier: Design of Sustainable Processes, 1917-1928. [NASA ADS] [CrossRef] [EDP Sciences] [MathSciNet] [PubMed]
  • Dudukovic M.P., Lee J.H. (1998) A comparison of the equilibrium and nonequilibrium models for a multicomponent reactive distillation column, Comput. Chem. Eng. 23, 1, 159-172. [NASA ADS] [CrossRef] [EDP Sciences] [MathSciNet] [PubMed]
  • Gear C.W. (1971) Simultaneous Numerical solution of differentialalgebraic equations, IEEE T. Circuit Theory 18, 89-95. [CrossRef]
  • Gorak A., Kenig E.Y., Schneider R. (2001) Reactive absorption: Optimal process design via optimal modelling, Chem. Eng. Sci. 56, 2, 343-350. [CrossRef]
  • Gorak A., Kreul L.U., Barton P.I. (1999a) Modelling of homogeneous reactive separation processes in packed columns, Chem. Eng. Sci. 54, 1, 19-24. [CrossRef]
  • Gorak A., Schneider R., Kenig E.Y. (1999b) Dynamic modelling of reactive absorption with the maxwell-stefan approach, T. I. Chem. Eng. A 77, 7, 633-638.
  • Higbie R. (1935) The Rate of Absorption of a Pure Gas into a Still Liquid during Short Periods of Exposure, T. Am. Inst. Chem. Eng. 31, 365-389.
  • Hikita H., Asai S., Takatsuka T. (1972) Gas Absorption with a Two-Step Instantaneous Chemical Reaction, Chem. Eng. J. 4, 1, 31-40. [CrossRef]
  • Lockett M.J. (1986) Distillation tray fundamentals, Cambridge University Press.
  • Newman J. (1991) Electrochemical systems, 2nd edition, Prentice- Hall, Englewood Cliffs, NJ.
  • Pagani G., d’Arminio Monforte A., Bianchi G. (2001) Transferbased models implementation in an equation oriented package, Comput. Chem. Eng. 25, 11-12, 1493-1511. [NASA ADS] [CrossRef] [EDP Sciences] [MathSciNet] [PubMed]
  • Prausnitz J., Lichtenthaler R., Gomes de Azevedo E. (1999) Molecular thermodynamics of fluid-phase equilibria, 3rd edition, Prentice Hall PTR, New Jersey.
  • Reid R.C., Prausnitz J.M., Poling B.E. (1987) Properties of gases and liquids, 4th edition, McGraw-Hill, New York.
  • Sawistowski H., Pilavakis P.A. (1979) Distillation with chemical reaction in a packed column, Inst. Chem. Eng. Symp. Series No. 56, London, 49-63.
  • Seader J.D., Henley E.J. (1981) Equilibrium stage separation operations in chemical engineering, Wiley, New York.
  • Slattery J.C. (1981) Momentum, energy and mass transfer in continua, 2nd edition, Krieger publishing company, Huntington, NY.
  • Smith W.R. (1980) The computation of chemical equilibria in complex systems, Ind. Eng. Chem. Fund. 19, 1-10. [CrossRef]
  • Taylor R., Krishna R. (1993) Multicomponent mass transfer, Wily series in chemical engineering.
  • Taylor R., Krishna R. (2000) Modelling reactive distillation, Chem. Eng. Sci. 55, 22, 5183-5229. [CrossRef]
  • Toor H.L. (1957) Diffusion in three component gas mixture, AIChE J. 3, 198-207. [CrossRef]
  • Valerio S., Vanni M., Baldi G. (1995) The role of non-ideal phenomena in interfacial mass transfer with chemical reaction, Chem. Eng. J. 57, 2, 205-217.
  • Versteeg G.F., Bosch H., Kuipers J.A.M., van Swaaij W.P.M. (1989) Mass transfer with complex chemical reactions, Gaz Separation Purification 3, 2, 75-83. [CrossRef]
  • Versteeg G.F., Huttenhuis P.J.G., Agrawal N.J., Hogendoorn J.A. (2007) Gas solubility of H2S and CO2 in aqueous solutions of N-methyldiethanolamine, J. Petrol. Sci. Eng. 55, 1-2, 122-134. [CrossRef]
  • Vignes A. (1966) Diffusion in binary solutions, Ind. Eng. Chem. Fund. 5, 189-199. [CrossRef]
  • Walas S.M. (1985) Phase equilibria in chemical engineering, Butterworth, Stoneham, MA.
  • Wesselingh J.A., Krishna R. (1997) The Maxwell-Stefan approach to mass transfer, Chem. Eng. Sci. 52, 6, 861-911. [CrossRef]

Current usage metrics show cumulative count of Article Views (full-text article views including HTML views, PDF and ePub downloads, according to the available data) and Abstracts Views on Vision4Press platform.

Data correspond to usage on the plateform after 2015. The current usage metrics is available 48-96 hours after online publication and is updated daily on week days.

Initial download of the metrics may take a while.