UvA-DARE (Digital Academic Repository) Mass transfer effects in distillation Springer, P.A.M. Link to publication

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1 UvA-DARE (Digital Academic Repository) Mass transfer effects in distillation Springer, P.A.M. Link to publication Citation for published version (APA): Springer, P. A. M. (2004). Mass transfer effects in distillation. General rights It is not permitted to download or to forward/distribute the text or part of it without the consent of the author(s) and/or copyright holder(s), other than for strictly personal, individual use, unless the work is under an open content license (like Creative Commons). Disclaimer/Complaints regulations If you believe that digital publication of certain material infringes any of your rights or (privacy) interests, please let the Library know, stating your reasons. In case of a legitimate complaint, the Library will make the material inaccessible and/or remove it from the website. Please Ask the Library: or a letter to: Library of the University of Amsterdam, Secretariat, Singel 425, 1012 WP Amsterdam, The Netherlands. You will be contacted as soon as possible. UvA-DARE is a service provided by the library of the University of Amsterdam ( Download date: 22 Mar 2019

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4 Krishnamurthy, R. and Taylor, R. (1985b). A nonequilibrium stage model of multicomponent separation processes. Part II: comparison with experiment. American Institute of Chemical Engineers Journal 31, Krishnamurthy, R. and Taylor, R. (1985c). A nonequilibrium stage model of multicomponent separation processes. Part III: the influence of unequal component efficiencies in process design problems. American Institute oj'chemical Engineers Journal 31, Lao, M. and Taylor, R. (1994). Modelling mass transfer in three-phase distillation. Industrial and Engineering Chemistry Research 24, Laroche, L., Bekiaris, N., Andersen, H.W. and Morari, M. (1992). The curious behaviour of homogeneous azeotropic distillation - implications for entrainer selection. American Institute of Chemical Engineers Journal 38, Levy, S.G., van Dongen, D.B. and Doherty, M.F. (1985). Design and synthesis of homogeneous azeotropic distillation. 2. Minimum reflux calculations for nonideal and azeotropic columns. Industrial and Engineering Chemistry: Fundamentals 24, Lewis, W.K. and Chang, K..C. (1928). Distillation III: the mechanism of rectification. Transactions of the American Institutions of Chemical Engineers 21, Li, Y., Chen, H. and Liu, J. (1999). Composition profile of an azeotropic continuous distillation with feed composition on a ridge or in a valley. Industrial and Engineering Chemistry Research 38, Lockett, M.J. (1986). Distillation tray fundamentals. Cambridge University Press, Cambridge. United Kingdom. Mehlhorn, A., Espuna, A., Bonsfills, A., Gorak, A. and Puigjaner, L. (1996). Modeling and experimental validation of both mass transfer and tray hydraulics in batch distillation. Computers & Chemical Engineering 20, S575-S580. Mendelson, H.D. (1967). The prediction of bubble terminal velocities from wave theory. American Institute of Chemical Engineers Journal 13, Michelsen, M.L. (1982a). The isothermal flash problem, Part I, Stability. Fluid Phase Equilibria 9, Michelsen, M.L. (1982b). The isothermal flash problem, Part II, Phase split calculation. Fluid Phase Equilibria 9, Muller, N.P. and Segura, H. (2000). An overall rate-based stage model for cross flow distillation columns. Chemical Engineering Science 55, Muller, D. and Marquardt, W. (1997). Experimental verification of multiple steady states in heterogeneous azeotropic distillation. Industrial and Engineering Chemistiy Research 36, Muller, D., Marquardt, W., Hauschild, T., Ronge, G. and Steude, H. (1997). Experimental validation of an equilibrium stage model for three-phase distillation. Maastricht, The Netherlands. Murphree, E.V. (1925). Rectifying column calculations with particular reference to n- component mixtures. Industrial and Engineering Chemistiy 17, Pacheco, M.A. and Rochelle, G.T. (1998). Rate-based modelling of reactive absorption of CO: and ELS into aqueous Methyldiethanolamine. Industrial and Engineering Chemistiy Research 37, Pagani, G., Monforte, A.A. and Bianchi, G. (2001). Transfer-based models implementation in an equation oriented package. Computers & Chemical Engineering 25, Pelkonen. S.. Kaesemann, R. and Gorak. A. (1997). Distillation lines for multicomponent separation in packed columns: theory and comparison with experiment. Industrial and Engineering Chemistiy Research 36,

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