Modelling reactive distillation

Modelling reactive distillation Modelling reactive distillation

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R. Taylor, R. Krishna / Chemical Engineering Science 55 (2000) 5183}5229 5229Congress on chemical engineering * ECCE-1, May 4}7, Florence,Vol. 2 (pp. 1423}1426).Thiel, C., Sundmacher, K., & Ho!mann, U. (1997a). Residue curve mapsfor heterogeneously catalysed reactive distillation of fuel ethersMTBE and TAME. Chemical Engineering Science, 52, 993}1005.Thiel, C., Sundmacher, K., & Ho!mann, U. (1997b). Synthesis of ETBE:Residue curve maps for the heterogeneously catalysed reactive distillationprocess. Chemical Engineering Journal, 66, 181}191.Tierney, J. W., & Riquelme, G. D. (1982). Calculation methods fordistillation systems with reaction. Chemical Engineering Communication,16, 91}108.Timofeev, V. S., Sera"mov, L. A., & Solokhin, A. V. (1994). Analysis ofreactive systems with selective exchange of material with the ambientmedium. Theoretical Foundations of Chemical Engineering, 28,416}420.Timofeev, V. S., Solokhin, A. V., & Kalerin, E. A. (1988). Multiplesteady states in the reaction-recti"cation process. Theoretical Foundationsof Chemical Engineering, 22, 488}492.Toor, H. L. (1965). Dual di!usion - reaction coupling in "rst ordermulticomponent systems. Chemical Engineering Science, 20,941}951.Towler, G. P., & Frey, S. J. (2000). Reactive distillation. In S. Kulprathipanja,Reactive separation processes. Philadelphia: Taylor andFrancis (Chapter 2).Trambouze, P. (1990). Countercurrent two-phase #ow "xed bed catalyticreactors. Chemical Engineering Science, 45, 2269}2275.Ung, S., & Doherty, M. F. (1995a). Vapor liquid phase equilibrium insystems with multiple chemical reactions. Chemical EngineeringScience, 50, 23}48.Ung, S., & Doherty, M. F. (1995b). Theory of phase equilibriain multireaction systems. Chemical Engineering Science, 50,3201}3216.Ung, S., & Doherty, M. F. (1995c). Calculation of residue curve mapsfor mixtures with multiple equilibrium chemical reactions. Industrialand Engineering Chemistry Research, 34, 3195}3202.Ung, S., & Doherty, M. F. (1995d). Necessary and su$cient conditionsfor reactive azeotropes in multireaction mixtures. American Instituteof Chemical Engineers Journal, 41, 2383}2392.Ung, S., & Doherty, M. F. (1995e). Synthesis of reactive distillationsystems with multiple equilibrium chemical reactions. Industrial andEngineering Chemistry Research, 34, 2555}2565.Velo, E., Puigjaner, L., & Recasens, F. (1988). Inhibition by product inthe liquid-phase hydration of iso-butene to tert-butyl alcohol * kineticsand equilibrium studies. Industrial and Engineering ChemistryResearch, 27, 2224}2231.Venimadhavan, G., Buzad, G., Doherty, M. F., & Malone, M. F.(1994). E!ect of kinetics on residue curve maps for reactive distillation.American Institute of Chemical Engineers Journal, 40,1814}1824.Venimadhavan, G., Malone, M. F., & Doherty, M. F. (1999a). Bifurcationstudy of kinetic e!ects in reactive distillation. American Instituteof Chemical Engineers Journal, 45, 546}556.Venimadhavan, G., Malone, M. F., & Doherty, M. F. (1999b). A noveldistillate policy for batch reactive distillation with application to theproduction of butyl acetate. Industrial and Engineering ChemistryResearch, 38, 714}722.Venkataraman, S., Chan, W. K., & Boston, J. F. (1990). Reactivedistillation using ASPEN PLUS. Chemical Engineering Progress,86(8), 45}54.Wajge, R. M., & Reklaitis, G. V. (1999). RDBOPT: A general purposeobject-oriented module for distributed campaign optimization ofreactive batch distillation. Chemical Engineering Journal, 75, 57}68.Walas, S. M. (1985). Phase equilibria in chemical engineering. Stoneham(MA): Butterworths.Wang, J. C., & Henke, G. E. (1966). Tridiagonal matrix for distillation.Hydrocarbon Processing, 45(8), 155}163, 45(9), 169Wang, J. C., & Wang, Y. L. (1980). A review on the modeling andsimulation of multi-stage separation processes. In W. D. Seider,& R. S. H. Mah, Foundations of computer aided chemical processdesign, vol. II (pp. 121}170).Wayburn, T. L., & Seader, J. D. (1987). Homotopy-continuationmethods for computer aided process design. Computers and ChemicalEngineering, 11, 7}25.Wiesner, U., Wittig, M., & Gorak, A. (1996). Design and optimization ofa nitric acid recovery plant from nitrous waste gases. Computers andChemical Engineering, 20, S1425}S1430.Xu, X., Zhao, Z., & Tian, S. -J. (1997). Study on catalytic distillationprocesses, Part III. Prediction of pressure drop and holdup incatalyst bed. Chemical Engineering Research and Design, Transactionsof the Institution of Chemical Engineers, Part A, 75, 625}629.Xu, X., Zhao, Z., & Tian, S. (1999). Study on catalytic distillationprocesses, Part IV: Axial dispersion of liquid in catalyst bed ofcatalytic distillation column. Chemical Engineering Research andDesign, Transactions of the Institution of Chemical Engineers, Part A,77, 16}20.Xu, Z., & Dudukovic, M. P. (1999). Modeling and simulation of a semibatchphoto reactive distillation. Chemical Engineering Science, 54,1397}1403.Yu, S., Zhou, A., & Tan, Q. (1997). Simulation of multistage catalyticstripping with a nonequilibrium stage model. Computers and ChemicalEngineering, 21, 409}415.Zheng, Y., & Xu, X. (1992a). Study on catalytic distillation processes,Part I: Mass transfer characteristics in catalyst bed within thecolumn. Chemical Engineering Research and Design, Transactions ofthe Institution of Chemical Engineers, Part A, 70, 459}546.Zheng, Y., & Xu, X. (1992b). Study on catalytic distillation processes,Part II: Simulation of catalytic distillation processes, Quasi homogeneousand rate based model. Chemical Engineering Research andDesign, Transactions of the Institution of Chemical Engineers, Part A,70, 465}470.Zhu, J., & Shen, F. (1995). The modelling and simulation of reactivedistillation processes. A.I.Ch.E. Symposium Series No. 304, vol. 91(pp. 297}300).

R. Taylor, R. Krishna / Chemical Engineering Science 55 (2000) 5183}5229 5229Congress on chemical engineering * ECCE-1, May 4}7, Florence,Vol. 2 (pp. 1423}1426).Thiel, C., Sundmacher, K., & Ho!mann, U. (1997a). Residue curve mapsfor heterogeneously catalysed <strong>reactive</strong> <strong>distillation</strong> of fuel ethersMTBE and TAME. Chemical Engineering Science, 52, 993}1005.Thiel, C., Sundmacher, K., & Ho!mann, U. (1997b). Synthesis of ETBE:Residue curve maps for the heterogeneously catalysed <strong>reactive</strong> <strong>distillation</strong>process. Chemical Engineering Journal, 66, 181}191.Tierney, J. W., & Riquelme, G. D. (1982). Calculation methods for<strong>distillation</strong> systems with reaction. Chemical Engineering Communication,16, 91}108.Timofeev, V. S., Sera"mov, L. A., & Solokhin, A. V. (1994). Analysis of<strong>reactive</strong> systems with selective exchange of material with the ambientmedium. Theoretical Foundations of Chemical Engineering, 28,416}420.Timofeev, V. S., Solokhin, A. V., & Kalerin, E. A. (1988). Multiplesteady states in the reaction-recti"cation process. Theoretical Foundationsof Chemical Engineering, 22, 488}492.Toor, H. L. (1965). Dual di!usion - reaction coupling in "rst ordermulticomponent systems. Chemical Engineering Science, 20,941}951.Towler, G. P., & Frey, S. J. (2000). Reactive <strong>distillation</strong>. In S. Kulprathipanja,Reactive separation processes. Philadelphia: Taylor andFrancis (Chapter 2).Trambouze, P. (1990). Countercurrent two-phase #ow "xed bed catalyticreactors. Chemical Engineering Science, 45, 2269}2275.Ung, S., & Doherty, M. F. (1995a). Vapor liquid phase equilibrium insystems with multiple chemical reactions. Chemical EngineeringScience, 50, 23}48.Ung, S., & Doherty, M. F. (1995b). Theory of phase equilibriain multireaction systems. Chemical Engineering Science, 50,3201}3216.Ung, S., & Doherty, M. F. (1995c). Calculation of residue curve mapsfor mixtures with multiple equilibrium chemical reactions. Industrialand Engineering Chemistry Research, 34, 3195}3202.Ung, S., & Doherty, M. F. (1995d). Necessary and su$cient conditionsfor <strong>reactive</strong> azeotropes in multireaction mixtures. American Instituteof Chemical Engineers Journal, 41, 2383}2392.Ung, S., & Doherty, M. F. (1995e). Synthesis of <strong>reactive</strong> <strong>distillation</strong>systems with multiple equilibrium chemical reactions. Industrial andEngineering Chemistry Research, 34, 2555}2565.Velo, E., Puigjaner, L., & Recasens, F. (1988). Inhibition by product inthe liquid-phase hydration of iso-butene to tert-butyl alcohol * kineticsand equilibrium studies. Industrial and Engineering ChemistryResearch, 27, 2224}2231.Venimadhavan, G., Buzad, G., Doherty, M. F., & Malone, M. F.(1994). E!ect of kinetics on residue curve maps for <strong>reactive</strong> <strong>distillation</strong>.American Institute of Chemical Engineers Journal, 40,1814}1824.Venimadhavan, G., Malone, M. F., & Doherty, M. F. (1999a). Bifurcationstudy of kinetic e!ects in <strong>reactive</strong> <strong>distillation</strong>. American Instituteof Chemical Engineers Journal, 45, 546}556.Venimadhavan, G., Malone, M. F., & Doherty, M. F. (1999b). A noveldistillate policy for batch <strong>reactive</strong> <strong>distillation</strong> with application to theproduction of butyl acetate. Industrial and Engineering ChemistryResearch, 38, 714}722.Venkataraman, S., Chan, W. K., & Boston, J. F. (1990). Reactive<strong>distillation</strong> using ASPEN PLUS. Chemical Engineering Progress,86(8), 45}54.Wajge, R. M., & Reklaitis, G. V. (1999). RDBOPT: A general purposeobject-oriented module for distributed campaign optimization of<strong>reactive</strong> batch <strong>distillation</strong>. Chemical Engineering Journal, 75, 57}68.Walas, S. M. (1985). Phase equilibria in chemical engineering. Stoneham(MA): Butterworths.Wang, J. C., & Henke, G. E. (1966). Tridiagonal matrix for <strong>distillation</strong>.Hydrocarbon Processing, 45(8), 155}163, 45(9), 169Wang, J. C., & Wang, Y. L. (1980). A review on the modeling andsimulation of multi-stage separation processes. In W. D. Seider,& R. S. H. Mah, Foundations of computer aided chemical processdesign, vol. II (pp. 121}170).Wayburn, T. L., & Seader, J. D. (1987). Homotopy-continuationmethods for computer aided process design. Computers and ChemicalEngineering, 11, 7}25.Wiesner, U., Wittig, M., & Gorak, A. (1996). Design and optimization ofa nitric acid recovery plant from nitrous waste gases. Computers andChemical Engineering, 20, S1425}S1430.Xu, X., Zhao, Z., & Tian, S. -J. (1997). Study on catalytic <strong>distillation</strong>processes, Part III. Prediction of pressure drop and holdup incatalyst bed. Chemical Engineering Research and Design, Transactionsof the Institution of Chemical Engineers, Part A, 75, 625}629.Xu, X., Zhao, Z., & Tian, S. (1999). Study on catalytic <strong>distillation</strong>processes, Part IV: Axial dispersion of liquid in catalyst bed ofcatalytic <strong>distillation</strong> column. Chemical Engineering Research andDesign, Transactions of the Institution of Chemical Engineers, Part A,77, 16}20.Xu, Z., & Dudukovic, M. P. (1999). Modeling and simulation of a semibatchphoto <strong>reactive</strong> <strong>distillation</strong>. Chemical Engineering Science, 54,1397}1403.Yu, S., Zhou, A., & Tan, Q. (1997). Simulation of multistage catalyticstripping with a nonequilibrium stage model. Computers and ChemicalEngineering, 21, 409}415.Zheng, Y., & Xu, X. (1992a). Study on catalytic <strong>distillation</strong> processes,Part I: Mass transfer characteristics in catalyst bed within thecolumn. Chemical Engineering Research and Design, Transactions ofthe Institution of Chemical Engineers, Part A, 70, 459}546.Zheng, Y., & Xu, X. (1992b). Study on catalytic <strong>distillation</strong> processes,Part II: Simulation of catalytic <strong>distillation</strong> processes, Quasi homogeneousand rate based model. Chemical Engineering Research andDesign, Transactions of the Institution of Chemical Engineers, Part A,70, 465}470.Zhu, J., & Shen, F. (1995). The modelling and simulation of <strong>reactive</strong><strong>distillation</strong> processes. A.I.Ch.E. Symposium Series No. 304, vol. 91(pp. 297}300).

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