Modelling reactive distillation
Tóm tắt
Từ khóa
Tài liệu tham khảo
Abufares, 1995, Mathematical modeling and simulation of an MTBE catalytic distillation process using SPEEDUP and AspenPlus, Chemical Engineering Research and Design, Transactions of the Institution on Chemical Engineers Part A, 73, 3
Agreda, 1990, High-purity methyl acetate via reactive distillation, Chemical Engineering Progress, 86, 40
Albet, J. M., Le Lann, J. M., Joulia, X., and Koehret, B. (1991). Rigorous simulation of multicomponent multisequence batch reactive distillation. Proceedings of COPE '91, Barcelona, Spain (pp. 75–80).
Alejski, 1991, Computation of the reacting distillation column using a liquid mixing model on the plates, Computers and Chemical Engineering, 15, 313, 10.1016/0098-1354(91)80005-G
Alejski, 1991, Analysis of complex chemical-reactions in distillation column. 1. Parallel reactions, Inzynieria Chemiczna i Procesowa, 12, 617
Alejski, 1996, Dynamic simulation of the multicomponent reactive distillation, Chemical Engineering Science, 51, 4237, 10.1016/0009-2509(96)00226-6
Alejski, 1988, Comparison of selected methods of reacting distillation column computing, Inzynieria Chemiczna i Procesowa, 10, 55
Alejski, 1989, Analysis of chemical-reaction course in distillation column, Inzynieria Chemiczna i Procesowa, 9, 565
Alejski, 1988, The application of a minimization method for solving reactive distillation problems, Computers and Chemical Engineering, 12, 833, 10.1016/0098-1354(88)80021-8
Allgor, 1996, Optimal batch process development, Computers and Chemical Engineering, 20, 885, 10.1016/0098-1354(95)00185-9
Altiqi, 1994, Steady-state rate-based modelling for CO2/amine absorption-desorption systems, Gas Separation and Purification, 8, 3, 10.1016/0950-4214(94)85002-X
Asselineau, L., Mikitenko, P., Viltard, J. C., & Zuliani, M. (1994) U.S. Patent 5368691: Reactive distillation process and apparatus for carrying it out
Babcock, P. D., & Clump, C. W. (1978). Distillation of chemically reactive solutions. In N.N. Li, Recent developments in separation science, vol. IV (pp. 149–166).
Backhaus, A. A. (1921). Continuous processes for the manufacture of esters, US patent 1400849.
Backhaus, A. A. (1922). Apparatus for producing high grade esters, US patent 1403224.
Backhaus, A. A. (1923a). Process for producing high grade esters, US patent 1454462.
Backhaus, A. A. (1923b). Process for esterification, US patent 1454463.
Balashov, 1981, Rules of primary reaction zone spread in continuous combined reaction-fractionation process, Theoretical Foundations of Chemical Engineering, 15, 406
Balashov, 1980, The statics analysis of continuous combined reaction-fractionation process, Theoretical Foundations of Chemical Engineering, 14, 803
Barbosa, 1987, Theory of phase diagrams and azeotropic conditions for two-phase reactive systems, Proceedings of the Royal Society London A, 413, 443, 10.1098/rspa.1987.0125
Barbosa, 1987, A new set of composition variables for the representation of reactive phase diagrams, Proceedings of the Royal Society London A, 413, 459, 10.1098/rspa.1987.0126
Barbosa, 1988, The influence of equilibrium chemical reactions on vapor liquid-phase diagrams, Chemical Engineering Science, 43, 529, 10.1016/0009-2509(88)87014-3
Barbosa, 1988, The simple distillation of homogeneous reactive mixtures, Chemical Engineering Science, 43, 541, 10.1016/0009-2509(88)87015-5
Barbosa, 1988, Design and minimum reflux calculations for single-feed multicomponent reactive distillation columns, Chemical Engineering Science, 43, 1523, 10.1016/0009-2509(88)85144-3
Barbosa, 1988, Design and minimum reflux calculations for double-feed multicomponent reactive distillation columns, Chemical Engineering Science, 43, 2377, 10.1016/0009-2509(88)85172-8
Barbosa, 1990, Theory of phase diagrams and azeotropic conditions for two-phase reactive systems, Proceedings of the Royal Society London A, 430, 669
Bart, 1996, Heterogene Reaktivdestillation mit axialer Rückvermischung, Chemie Ingenieur Technik, 68, 944, 10.1002/cite.330680809
Bart, 1995, Distillation with chemical-reaction and apparatus selection, Separaration Science and Technology, 30, 1849, 10.1080/01496399508010380
Bart, 1997, Der Hybridprozess Reaktivdestillation/Pervaporation zur Herstellung von Carbonsäureestern, Chemie Ingenieur Technik, 69, 824, 10.1002/cite.330690613
Bartlett, D. A., & Wahnschafft, O. M. (1998). Dynamic simulation and control strategy evaluation for MTBE reactive distillation. In J.F. Pekny & G.E. Blau, Foundations of computer-aided process operation, AIChE Symposium Series, vol. 320, (pp. 315–321).
Van Baten, 2000, Modelling of sieve tray hydraulics using computational fluid dynamics, Chemical Engineering Journal, 77, 143, 10.1016/S1385-8947(99)00164-3
Baur, 1999, Comparison of equilibrium stage and nonequilibrium stage models for reactive distillation, Chemical Engineering Journal, 76, 33, 10.1016/S1385-8947(99)00114-X
Belck, 1955, Continuous reactions in distillation equipment, American Institute of Chemical Engineers Journal, 1, 467, 10.1002/aic.690010414
Berman, 1948, Esterification. Continuous production of Dibutyl phthalate in a distillation column, Industrial and Engineering Chemistry, 40, 2139, 10.1021/ie50467a027
Berman, 1948, Dibutyl phthalate. Reaction rate of catalytic esterification, Industrial and Engineering Chemistry, 40, 1312, 10.1021/ie50463a030
Bessling, 1998, Investigations on the synthesis of methyl acetate in a heterogeneous reactive distillation process, Chemical Engineering and Technolgy, 21, 393, 10.1002/(SICI)1521-4125(199805)21:5<393::AID-CEAT393>3.0.CO;2-9
Bessling, 1997, Design of processes with reactive distillation line diagrams, Industrial and Engineering Chemistry Research, 36, 3032, 10.1021/ie960727p
Bessling, B., Schembecker, G., & Simmrock, K. H. (1997b). Design of reactive distillation processes with reactive and nonreactive distillation zones. Distillation and absorption '97, Institute of Chemical Engineers Symposium Series, vol. 142 (pp. 675–684).
Bezzo, 1999, Steady-state analysis of an industrial reactive distillation column, Separation and Purification Technology, 16, 251, 10.1016/S1383-5866(99)00016-7
Block, 1977, Carrying out continuous reactions with superposed distillation, Chemie Ingenieur Technik, 49, 151, 10.1002/cite.330490215
Block, 1977, Simulationsmethode fur homogene Flussigphasenreacktion mit uberlagerter Destillation, Verfahrenstechnik, 11, 101
Bock, H., & Wozny, G. (1997). Analysis of distillation and reaction rate in reactive distillation. Distillation and absorption '97. Institute of Chemical Engineers Symposium Series, vol. 142 (pp. 553–564).
Bogacki, 1989, The fast method of the solution of a reacting distillation problem, Computers and Chemical Engineering, 13, 1081, 10.1016/0098-1354(89)87049-8
Bollyn, 1998, Development of a reactive process model for a batch reactive distillation — a case study, Computers and Chemical Engineering, 22, S87, 10.1016/S0098-1354(98)00041-6
Bondy, R. W. (1991) Physical continuation approaches to solving reactive distillation problems. Paper presented at the AIChE meeting, Los Angeles.
Bravo, 1993, Investigations in a catalytic distillation pilot plant, Industrial and Engineering Chemistry Research, 32, 2220, 10.1021/ie00022a004
Buchholz, M., Pinaire, R., & Ulowetz, M. A. (1995). Structure and method for catalytically reacting fluid streams in mass transfer apparatus, European patent 448884B1.
Buzad, 1994, Design of three component kinetically controlled reactive distillation systems using fixed-point methods, Chemical Engineering Science, 49, 1947, 10.1016/0009-2509(94)80079-0
Buzad, 1995, New tools for the design of kinetically controlled reactive distillation columns for ternary mixtures, Computers and Chemical Engineering, 19, 395, 10.1016/0098-1354(94)00068-Y
Carey, 1991, A model of acid gas absorption/stripping using MDEA with added acid, Gas Separation and Purification, 5, 95, 10.1016/0950-4214(91)80006-Q
Carland, R. J. (1994). Fractionation tray for catalytic distillation, US patent 5308451.
Carra, 1979, Synthesis of propylene oxide from propylene chlorohydrins — II. Modeling of the distillation with chemical reaction unit, Chemical Engineering Science, 34, 1133, 10.1016/0009-2509(79)85019-8
Carra, 1979, Synthesis of propylene oxide from propylene-chlorohydrins — I Kinetic aspects of the process, Chemical Engineering Science, 34, 1123, 10.1016/0009-2509(79)85018-6
Chang, 1988, Simulation of continuous reactive distillation by a homotopy continuation method, Computers and Chemical Engineering, 12, 1243, 10.1016/0098-1354(88)85074-9
Ciric, 1994, Synthesis of nonequilibrium reactive distillation by MINLP optimization, American Institute of Chemical Engineers Journal, 40, 1479, 10.1002/aic.690400907
Ciric, 1994, Steady-state multiplicities in an ethylene glycol reactive distillation column, Industrial and Engineering Chemistry Research, 33, 2738, 10.1021/ie00035a025
Ciric, A. R., & Spencer, J. (1995). Shortcut calculations in reactive distillation. Paper 21d, AIChE National Meeting, Miami Beach.
Cleary, 1985, Separation of closely boiling mixtures by reactive distillation. 2. Experiments, Industrial and Engineering Chemistry Process Design & Development, 24, 1071, 10.1021/i200031a029
Cornelisse, 1980, Numerical calculation of simultaneous mass transfer of two gasses accompanied by complex reversible reactions, Chemical Engineering Science, 35, 1245, 10.1016/0009-2509(80)85116-5
Corrigan, 1969, A development study of methanol acetic acid esterification, Canadian Journal of Chemical Engineering, 47, 334, 10.1002/cjce.5450470404
Corrigan, 1968, Effect of distillation on a chemical reaction, Industrial and Engineering Chemistry Research Process Design and Development, 7, 383, 10.1021/i260027a012
Crossland, C. S., Gildert, G. R., & Hearn, D. (1995). Catalytic distillation structure, US patent 5431890.
Cuille, 1986, Dynamic simulation of multicomponent batch rectification with chemical reactions, Computers and Chemical Engineering, 10, 389, 10.1016/0098-1354(86)87009-0
Danckwerts, 1970
Davies, 1979, Distillation with chemical reaction — the distillation of formaldehyde solutions in a sieve plate column, Institute of Chemical Engineers Symposium Series, 56, 65
Deuflhard, 1987, One-step and extrapolation methods for differential-algebraic equations, Numerical Mathematics, 51, 501, 10.1007/BF01400352
DeGarmo, 1992, Consider reactive distillation, Chemical Engineering Progress, 3, 43
Doherty, 1990, Topological theory of phase diagrams for reacting mixtures, Proceedings of the Royal Society London A, 430, 669, 10.1098/rspa.1990.0112
Doherty, 1992, Reactive distillation by design, Chemical Engineering Research and Design, Transactions of the Institution of Chemical Engineers, Part A, 70, 448
Doherty, 1994, New tools for the design of kinetically controlled reactive distillation columns, Computers and Chemical Engineering, 18, S1, 10.1016/0098-1354(94)80003-0
Duprat, 1988, Reactive distillation process optimization by empirical formulae construction, Computers and Chemical Engineering, 11, 1141, 10.1016/0098-1354(88)87035-2
Duprat, 1991, Reactive distillation of pyridine mixtures with an organic acid. I. Determination of the reactive distillation equilibrium, Canadian Journal of Chemical Engineering, 69, 1320, 10.1002/cjce.5450690612
Duprat, 1991, Reactive distillation of pyridine mixtures with an organic acid. II. Parametric sensitivity and optimization of the process, Canadian Journal of Chemical Engineering, 69, 1327, 10.1002/cjce.5450690613
Egly, 1979, Optimum design and operation of batch rectification accompanied by chemical reaction, Computers and Chemical Engineering, 3, 169, 10.1016/0098-1354(79)80028-9
Eldarsi, 1998, Methyl-tert-butyl ether catalytic distillation column. Part I: Multiple steady-states, Chemical Engineering Research and Design, Transactions of the Institution of Chemical Engineers, Part A, 76, 509, 10.1205/026387698524983
Eldarsi, 1998, Methyl-tert-butyl ether catalytic distillation column. Part II, Chemical Engineering Research and Design, Transactions of the Institution of Chemical Engineers, Part A, 76, 517, 10.1205/026387698524992
Ellenberger, 1999, Counter-current operation of structured catalytically packed distillation columns, Chemical Engineering Science, 54, 1339, 10.1016/S0009-2509(99)00055-X
Espinosa, 1999, Analysis of finishing reactive distillation columns, Industrial and Engineering Chemistry Research, 38, 187, 10.1021/ie9707073
Espinosa, 1995, Some aspects in the design of multicomponent reactive distillation columns including non reactive species, Chemical Engineering Science, 50, 469, 10.1016/0009-2509(94)00258-S
Espinosa, 1995, Product composition regions of single feed reactive distillation column, Industrial and Engineering Chemistry Research, 34, 853, 10.1021/ie00042a017
Espinosa, 1996, Some aspects in the design of multicomponent reactive distillation columns with a reacting core, Industrial and Engineering Chemistry Research, 35, 4537, 10.1021/ie960355k
Espinosa, 1994, Dynamic behavior of reactive distillation columns, equilibrium systems, Chemical Engineering Communications, 128, 19, 10.1080/00986449408936234
Espinosa, 1993, Graphical procedure for reactive distillation systems, Chemical Engineering Communications, 119, 109, 10.1080/00986449308936110
Fair, 1998, Design aspects for reactive distillation — columns for simultaneous reaction and separation need skilful planning, Chemical Engineering (New York), 105, 158
Feinberg, 1999, Recent results in optimal reactor synthesis via attainable region theory, Chemical Engineering Science, 54, 2535, 10.1016/S0009-2509(98)00461-8
Feinberg, 1997, Optimal reactor design from a geometric viewpoint — I. Universal properties of the attainable region, Chemical Engineering Science, 52, 1637, 10.1016/S0009-2509(96)00471-X
Flato, 1992, Development and start-up of a fixed bed reaction column for manufacturing antiknock enhancer MTBE, Chemical Engineering and Technology, 15, 193, 10.1002/ceat.270150308
Frank, 1995, Modeling of simultaneous mass and heat transfer with chemical reaction using the Maxwell Stefan theory — II. Non-isothermal study, Chemical Engineering Science, 50, 1661, 10.1016/0009-2509(95)00011-S
Frank, 1995, Modeling of simultaneous mass and heat transfer with chemical reaction using the Maxwell Stefan theory — I. Model development and isothermal study, Chemical Engineering Science, 50, 1645, 10.1016/0009-2509(95)00012-T
Frey, S. J., Ozmen, S. M., Hamm, D. A., Pinjala, V., & DeGarmo, J. L. (1993). Advanced ether technology commercialised. Paper presented at the world conference on clean fuels and air quality control, Washington, DC.
Frey, 1999, Thermodynamic fundamentals of reactive distillation, Chemical Engineering and Technology, 22, 11, 10.1002/(SICI)1521-4125(199901)22:1<11::AID-CEAT11>3.0.CO;2-6
Frey, 1999, Reactive azeotropes in kinetically controlled reactive distillation, Chemical Engineering Research and Design, Transactions of the Institution of Chemical Engineers, Part A, 77, 613, 10.1205/026387699526656
Fuchigami, 1990, Hydrolysis of methyl acetate in distillation column packed with reactive packing of ion exchange resin, Journal of Chemical Engineering Japan, 23, 354, 10.1252/jcej.23.354
Gani, 1998, A generalized reactive separation unit model. Modelling and simulation aspects, Computers and Chemical Engineering, 22, S363, 10.1016/S0098-1354(98)00076-3
Gaspillo, 1999, Dehydrogenation of 2-propanol in reactive distillation column for chemical heat pump, Journal of Chemical Engineering Japan, 31, 440, 10.1252/jcej.31.440
Gehrke, 1997, A singularity theory approach to the study of reactive distillation, Computers and Chemical Engineering, 21, S1001, 10.1016/S0098-1354(97)87633-8
Gelbein, A. P., & Buchholz, M. (1991). Process and structure for effecting catalytic reactions in distillation structure, US patent 5073236.
Giessler, 1998, Feasibility study of reactive distillation using the analysis of statics, Industrial and Engineering Chemistry Research, 37, 2220, 10.1021/ie980277w
Giessler, 1999, Feasibile separation modes for various reactive distillation systems, Industrial and Engineering Chemistry Research, 38, 4060, 10.1021/ie9900162
Glasscock, 1989, Numerical simulation of theories for gas absorption with chemical reaction, American Institute of Chemical Engineers Journal, 35, 1271, 10.1002/aic.690350806
Glasser, 1997, Reactor and process synthesis, Computers and Chemical Engineering, 21, S775, 10.1016/S0098-1354(97)87597-7
Gonzalez, 1997, Preparation of tertiary amyl alcohol in a reactive distillation column.1. Reaction kinetics, chemical equilibrium, and mass-transfer issues, Industrial and Engineering Chemistry Research, 36, 3833, 10.1021/ie960749b
Gonzalez, 1997, Preparation of tert-amyl alcohol in a reactive distillation column.2. Experimental demonstration and simulation of column characteristics, Industrial and Engineering Chemistry Research, 36, 3845, 10.1021/ie960808l
Grosser, 1987, Modeling of reactive distillation systems, Industrial and Engineering Chemistry Research, 26, 983, 10.1021/ie00065a023
Groten, W. A., Booker, D., & Crossland, C. S. (1998). Catalytic distillation structure, US patent 5730843.
van Gulijk, 1998, Using computational fluid dynamics to calculate transversal dispersion in a structured packed bed, Computers and Chemical Engineering, 22, S767, 10.1016/S0098-1354(98)00144-6
Gumus, 1997, Reactive distillation column design with vapor/liquid/liquid equilibria, Computers and Chemical Engineering, 21, S983, 10.1016/S0098-1354(97)87630-2
Güttinger, T. E. (1998). Multiple steady states in azeotropic and reactive distillation. Dissertation ETH No. 12720, Swiss Federal Institute of Technology (ETH), Zurich.
Güttinger, 1997, Predicting multiple steady states in distillation, Computers and Chemical Engineering, 21, S995, 10.1016/S0098-1354(97)87632-6
Güttinger, 1999, Predicting multiple steady states in equilibrium reactive distillation. 1. Analysis of nonhybrid systems, Industrial and Engineering Chemistry Research, 38, 1633, 10.1021/ie980327x
Güttinger, 1999, Predicting multiple steady-states in equilibrium reactive distillation. 2. Analysis of hybrid systems, Industrial and Engineering Chemistry Research, 38, 1649, 10.1021/ie980328p
Van Hasselt, B. (1999). The three-levels-of-porosity reactor. Ph.D. dissertation in Chemical Engineering, Delft University of Technology.
Hauan, S. (1998). On the behaviour of reactive distillation systems. Doctoral thesis, Norwegian University of Science and Technology, Trondheim.
Hauan, 1995, Why methyl-tert-butyl-ether production by reactive distillation may yield multiple solutions, Industrial and Engineering Chemistry Research, 34, 987, 10.1021/ie00042a037
Hauan, 1997, Multiplicity in reactive distillation of MTBE, Computers and Chemical Engineering, 21, 1117, 10.1016/S0098-1354(96)00322-5
Hauan, 1999, An introduction to reactive distillation, Chemical Technology (RSA), 8
Hauan, 1996, Geometric visualization of reactive fixed points, Computers and Chemical Engineering, 20, S133, 10.1016/0098-1354(96)00033-6
Hauan, 1998, A phenomena based design approach to reactive distillation, Chemical Engineering Research and Design, Transactions of the Institution of Chemical Engineers, Part A, 76, 396, 10.1205/026387698524820
Hauan, 1997, Dynamic evidence of the multiplicity mechanism in methyl tert-butyl ether reactive distillation, Industrial and Engineering Chemistry Research, 36, 3995, 10.1021/ie970237c
Hauan, 2000, Difference points in extractive and reactive cascades. I — basic properties and analysis, Chemical Engineering Science, 55, 3145, 10.1016/S0009-2509(99)00591-6
Hauan, 2000, Phenomena-based analysis of fixed points in reactive separation systems, Chemical Engineering Science, 55, 1053, 10.1016/S0009-2509(99)00392-9
Hearn, D. (1993). Catalytic distillation machine, US patent 5266546.
Henley, 1981
Higler, 1999, Counter-current operation of a structured catalytically packed bed reactor, Chemical Engineering Science, 54, 5145, 10.1016/S0009-2509(99)00229-8
Higler, 1998, Modeling of a reactive separation process using a nonequilibrium stage model, Computers and Chemical Engineering, 22, S111, 10.1016/S0098-1354(98)00044-1
Higler, 1999, Nonequilibrium Modelling of reactive distillation, Chemical Engineering Science, 54, 1389, 10.1016/S0009-2509(99)00056-1
Higler, 1999, The influence of mass transfer and liquid mixing on the performance of reactive distillation tray column, Chemical Engineering Science, 54, 2873, 10.1016/S0009-2509(98)00317-0
Higler, 1999, A nonequilibrium cell model for multicomponent (reactive) separation processes, American Institute of Chemical Engineers Journal, 45, 2357, 10.1002/aic.690451111
Higler, 1999, A non-equilibrium cell model for packed distillation columns. The influence of maldistribution, Industrial and Engineering Chemistry Research, 38, 3988, 10.1021/ie990261l
Higler, 2000, Non-equilibrium modelling of reactive distillation: A dusty fluid model for heterogeneously catalysed processes, Industrial and Engineering Chemistry Research, 39, 1596, 10.1021/ie990547q
Holland, 1963
Holland, 1981
Hu, 1999, Simulation and optimization of a coupled reactor/column system for trioxane synthesis, Chemical Engineering Science, 54, 1353, 10.1016/S0009-2509(99)00072-X
Huang, 1998, A study of mass transfer behaviour in a catalytic distillation column, Canadian Journal of Chemical Engineering, 76, 323, 10.1002/cjce.5450760222
Huang, 1998, Application of catalytic distillation for the aldol condensation of acetone, Chemical Engineering Science, 53, 3489, 10.1016/S0009-2509(98)00157-2
Hunek, 1979, Methods for calculating reactive distillation, International Chemical Engineering, 19, 248
Ilme, J. K., Keskinen, K. I., Markkanen, V. L., Aittamaa, J. R. (1997). Simulation of industrial MTBE distillation column using an equilibrium stage model with efficiency calculation. Distillation and absorption '97, Institute of Chemical Engineers Symposium Series, vol. 142 (pp. 497–510).
Isla, 1996, Modeling, analysis, and simulation of a methyl tert-butyl ether reactive distillation column, Industrial and Engineering Chemistry Research, 35, 2396, 10.1021/ie9505930
Ismail, 1999, Synthesis of reactive and combined reactor/separation systems utilizing a mass/heat exchange transfer module, Chemical Engineering Science, 54, 2721, 10.1016/S0009-2509(98)00331-5
Izarraz, 1980, Solve more distillation problems, Part 9 — when reactions occur, Hydrocarbon Processing, 59, 195
Jackson, 1977
Jacobs, 1993, Multiple solutions in reactive distillation for methyl-tert-butyl ether synthesis, Industrial and Engineering Chemistry Research, 32, 1706, 10.1021/ie00020a025
Jelinek, 1976, Steady state countercurrent equilibrium stage separation with chemical reaction by relaxation method, Chemical Engineering Communications, 2, 79, 10.1080/00986447608960449
Johnson, K. H. (1993). Catalytic distillation structure, US patent 5189001.
Johnson, K. H., & Dallas, A. B. (1994). Catalytic distillation structure, US patent 5348710.
Jones, Jr., E. M. (1985). Contact structure for use in catalytic distillation, US patent 4536373.
Jones, Jr., E. M. (1992a). Catalytic distillation reactor, US patent 5130102.
Jones, Jr., E. M. (1992b). Distillation column reactor, European patent 0 402 019 A3.
Kaibel, 1979, Reactions in distillation columns, German Chemical Engineering, 2, 180
Karpilovsky, O. L., Pisarenko, Y. A., & Serafimov, L. A. (1997). Multiple solutions in single-product reactive distillation. Distillation and absorption '97, Institute of Chemical Engineers Symposium Series vol. 142 (pp. 685–694).
Kenig, 1995, A film model based approach for simulation of multicomponent reactive separation processes, Chemical Engineering and Processing, 34, 97, 10.1016/0255-2701(94)03004-9
Kenig, 1997, Modeling of reactive absorption using the Maxwell–Stefan equations, Industrial and Engineering Chemistry Research, 36, 4325, 10.1021/ie970186j
Kenig, 1999, An integrated tool for synthesis and design of reactive distillation, Chemical Engineering Science, 54, 1347, 10.1016/S0009-2509(99)00071-8
Keyes, 1932, Esterification processes and equipment, Industrial and Engineering Chemistry, 24, 1096, 10.1021/ie50274a003
Kinoshita, 1985, Simulation procedure for multistage water/hydrogen exchange column for heavy water enrichment accounting for catalytic and scrubbing efficiencies, Journal of Nuclear Science and Technology, 22, 398, 10.1080/18811248.1985.9735673
Kinoshita, 1983, A new simulation procedure for multicomponent distillation column processing nonideal solutions or reactive solutions, Journal of Chemical Engineering Japan, 16, 370, 10.1252/jcej.16.370
Kolah, 1996, Acetalization of formaldehyde with methanol in batch and continuous reactive distillation, Industrial and Engineering Chemistry Research, 35, 3707, 10.1021/ie950563x
Komatsu, 1977, Application of the relaxation method of solving reacting distillation problems, Journal of Chemical Engineering Japan, 10, 200, 10.1252/jcej.10.200
Komatsu, 1977, A new method of convergence for solving reacting distillation problems, Journal of Chemical Engineering Japan, 10, 292, 10.1252/jcej.10.292
Kooijman, 1995, A dynamic nonequilibrium model of tray distillation columns, American Institute of Chemical Engineers Journal, 41, 1852, 10.1002/aic.690410804
Krafczyk, 1994, Einsatz von Katalysatorpakungen fuer die Herstellung von Methylacetat durch reactive Rektifikation, Chemie Ingenieur Technik, 66, 1372, 10.1002/cite.330661014
Kreul, 1999, Modeling of homogeneous reactive separation processes in packed columns, Chemical Engineering Science, 54, 19, 10.1016/S0009-2509(98)00239-5
Kreul, 1999, Dynamic rate-based model for multicomponent batch distillation, American Institute of Chemical Engineers Journal, 54, 1953, 10.1002/aic.690450912
Kreul, 1998, Dynamic catalytic distillation, Computers and Chemical Engineering, 22, S371, 10.1016/S0098-1354(98)00077-5
Krishna, 1999, CFD simulations of sieve tray hydrodynamics, Chemical Engineering Research and Design, Transactions of the Institution of Chemical Engineers, Part A, 77, 639, 10.1205/026387699526575
Krishna, 1994, Strategies for multiphase reactor selection, Chemical Engineering Science, 49, 4029, 10.1016/S0009-2509(05)80005-3
Krishna, 1997, The Maxwell–Stefan approach to mass transfer, Chemical Engineering Science, 52, 861, 10.1016/S0009-2509(96)00458-7
Krishnamurthy, 1985, A Nonequilibrium stage model of multicomponent separation processes, American Institute of Chemical Engineers Journal, 32, 449, 10.1002/aic.690310312
Kumar, 1999, Modeling, analysis and control of ethylene glycol reactive distillation column, American Institute of Chemical Engineers Journal, 45, 51, 10.1002/aic.690450106
Lebens, P. J. M. (1999). Development and design of a monolith reactorfor gas–liquid countercurrent operation. Ph.D. dissertation, Delft University of Technology, Delft.
Lee, 1998, A comparison of the equilibrium and nonequilibrium models for a multicomponent reactive distillation column, Computers and Chemical Engineering, 23, 159, 10.1016/S0098-1354(98)00257-9
Lee J. H., & Dudukovic, M. P. (1999). Dynamic simulation of a reactive distillation tray column using a rate-based model. Paper presented at AIChE National meeting, Dallas.
Lee, J. W., Hauan, S., Lien, K. M., & Westerberg, A. W. (2000a). Graphical methods for designing reactive distillation columns. I — The Ponchon–Savarit Diagram. Proceedings of the Royal Society London A, in press.
Lee, J. W., Hauan, S., Lien, K. M., & Westerberg, A. W. (2000b). Graphical methods for designing reactive distillation columns. I — The McCabe–Thiele Diagram. Proceedings of the Royal Society London A, in press.
Lee, 2000, Difference points in extractive and reactive cascades. II — Generating design alternatives by the lever rule for reactive systems, Chemical Engineering Science, 55, 3161, 10.1016/S0009-2509(99)00590-4
Lee, 2000, Reaction distribution in a reactive distillation column by graphical methods, American Institute of Chemical Engineers Journal, 46, 1218, 10.1002/aic.690460614
Lee, 2000, Circumventing an azeotrope in reactive distillation, Industrial and Engineering Chemistry Research, 39, 1061, 10.1021/ie990447k
Leyes, C. E., & Othmer, D. F. (1945a). Continuous esterification of butanol and acetic acid, kinetic and distillation considerations. Transactions of the American Institute of Chemical Engineers, 41, 157–196, 481.
Leyes, 1945, Esterification of butanol and acetic acid, Industrial and Engineering Chemistry, 37, 968, 10.1021/ie50430a021
Lockett, 1986
Machietto, S., & Mujtaba, I. (1992). Design and operation policies for batch distillation. Proceedings of NATO ASI on batch processing systems engineering, Antalya, Turkey, May 29–June 7.
Mahajani, 1999, Kinetic azeotropy and design of reactive distillation columns, Industrial and Engineering Chemistry Research, 38, 177, 10.1021/ie9802663
Mahajani, 1999, Design of reactive distillation columns for multicomponent kinetically controlled reactive systems, Chemical Engineering Science, 54, 1425, 10.1016/S0009-2509(99)00080-9
Mahajani, S. M., & Kolah, A. K. (1996). Some design aspects of reactive distillation columns (RDC). Industrial and Engineering Chemistry Research, 35, 4587–4596; additions and corrections. Industrial and Engineering Chemistry Research, 36, 2520.
Marek, 1954, Rectification with a chemical reaction. I. Calculation of the number of theoretical plates for continuous plate columns, Collection of Czechoslovak Chemical Communications, 19, 1055, 10.1135/cccc19541055
Marek, 1956, Rectification with a chemical reaction. II. Plant rectification of mixtures of water, acetic acid, acetic anhydride, Collection of Czechoslovak Chemical Communications, 21, 1560, 10.1135/cccc19561560
Marion, M. C., Viltard, J. C., Travers, P., Harter, I., & Forestiere, A. (1998). Process and apparatus for reactive distillation with a particular distribution of liquid and vapor phases, US patent 5776320.
Mason, 1983
McDonald, 1997, GLOPEQ: A new computational tool of the phase and chemical equilibrium problem, Computers and Chemical Engineering, 21, 1, 10.1016/0098-1354(95)00250-2
McGregor, C., Glasser, D., & Hildebrandt, D. (1997) Process synthesis of a reactive distillation system using attainable region results. Distillation and absorption '97, Institue of Chemical Engineers Symposium Series, vol. 142 (pp. 663–674).
Melles, 2000, Optimisation of the conceptual design of reactive distillation columns, Chemical Engineering Science, 55, 2089, 10.1016/S0009-2509(99)00497-2
Moe, 1995, Dynamic model of a system with phase and reaction equilibrium, Computers and Chemical Engineering, 19, S513, 10.1016/0098-1354(95)00067-C
Mohl, 1998, Multiple steady states in a reactive distillation column for the production of the fuel ether TAME I. Theoretical analysis, Chemical Engineering and Technology, 21, 133, 10.1002/(SICI)1521-4125(199802)21:2<133::AID-CEAT133>3.0.CO;2-G
Mohl, 1997, Nonlinear dynamics of reactive distillation processes for the production of fuel ethers, Computers and Chemical Engineering, 21, S989, 10.1016/S0098-1354(97)00178-6
Mohl, 1999, Steady-state multiplicities in reactive distillation columns for the production of fuel ethers MTBE and TAME, Chemical Engineering Science, 54, 1029, 10.1016/S0009-2509(98)00327-3
Mommessin, 1980, Solve more distillation problems, part 10 — another way to handle reactions, Hydrocarbon Processing, 59, 144
Mommessin, 1983, Solve more distillation problems, part 13 — multiple columns with reactions, Hydrocarbon Processing, 62, 195
Moritz, 1999, Fluid dynamics in reactive distillation packing Katapak®-S, Chemical Engineering Science, 54, 1367, 10.1016/S0009-2509(99)00078-0
Mujtaba, I., & Machietto, S. (1992). Optimal operation of reactive batch distillation process. American Institute of Chemical Engineers annual meeting, Miami Beach.
Nelson, 1971, Countercurrent equilibrium stage separation with reaction, American Institute of Chemical Engineers Journal, 17, 1043, 10.1002/aic.690170506
Neumann, 1984, Recovery of dilute acetic acid by esterification in a packed chemorectification column, Industrial and Engineering Chemistry Process Design and Development, 23, 654, 10.1021/i200027a005
Nijhuis, 1993, Multiple steady states during reactive distillation of methyl-tert-butyl-ether, Industrial and Engineering Chemistry Research, 32, 2767, 10.1021/ie00023a045
Nisoli, 1997, Attainable regions for reaction with separation, American Institute of Chemical Engineers Journal, 43, 374, 10.1002/aic.690430211
Nocca, J. L., Leonard, J., Gaillard, J. F., & Amigues, P. (1989). Process for manufacturing a tertiary alkyl ether by reactive distillation, US patent 4847431.
Nocca, J. L., Leonard, J., Gaillard, J. F., & Amigues, P. (1991). Apparatus for reactive distillation, US patent 5013407.
Okasinski, 1997, Thermodynamic behavior of reactive azeotropes, American Institute of Chemical Engineers Journal, 43, 2227, 10.1002/aic.690430909
Okasinski, M. J., & Doherty, M. F. (1997). Effects of unfavorable thermodynamics on reactive distillation column design. Distillation and absorption '97, Institue of Chemical Engineers Symposium Series, vol. 142 (pp. 695–704).
Okasinski, 1998, Design method for kinetically controlled, staged reactive distillation columns, Industrial and Engineering Chemistry Research, 37, 2821, 10.1021/ie9708788
Onda, 1968, Mass transfer coefficients between gas and liquid phases in packed columns, Journal of Chemical Engineering Japan, 1, 56, 10.1252/jcej.1.56
Oost, 1996, The synthesis of tertiary amyl methyl ether (TAME), Chemical Engineering Science, 51, 329, 10.1016/0009-2509(95)00258-8
Oost, 1995, The synthesis of tertiary amyl methyl ether (TAME), Chemical Engineering and Technology, 18, 110, 10.1002/ceat.270180205
Oudshoorn, O. L. (1999) Zeolite coatings applied in structured catalyst packings. Ph.D. dissertation, Delft University of Technology, Delft.
Papalexandri, 1996, Generalized modular representation framework for process synthesis, American Institute of Chemical Engineers Journal, 42, 1010, 10.1002/aic.690420413
Patlasov, 1996, Qualitative analysis of the mathematical model for the dynamics of multicomponent batch reactive rectification, Theoretical Foundations of Chemical Engineering, 30, 81
Pekkanen, M. (1995a). Pinches in reactive distillation: Conditions of existence. A.I.Ch.E. Symposium Series No. 304, vol. 91 (pp. 301–304).
Pekkanen, 1995, A local optimzation method for the design of reactive distillation, Computers and Chemical Engineering, 19, S235, 10.1016/0098-1354(95)00078-G
Pelkonen, S., Gorak, A., Kooijman, H. A., & Taylor, R. (1997). Operation of a packed distillation column: Modelling and experiments distillation. Distillation and absorption '97, Institute of Chemical Engineers Symposium Series, vol. 142 (pp. 269–277).
Perez-Cisneros, 1997, Reactive separation systems. Part I, Chemical Engineering Science, 52, 527, 10.1016/S0009-2509(96)00424-1
Perez-Cisneros, E., Schenk, M., & Gani, R. (1997b). A new approach to reactive distillation simulation. Distillation and absorption '97, Institue of Chemical Engineers Symposium Series, 142 (pp. 715–724).
Perez-Cisneros, 1996, Aspects of simulation, design and analysis of reactive distillation operations, Computers and Chemical Engineering, 20, S267, 10.1016/0098-1354(96)00055-5
Pilavachi, 1997, Modeling and simulation of reactive distillation operations, Industrial and Engineering Chemistry Research, 36, 3188, 10.1021/ie9606404
Pinjala, V., DeGarmo, J. L., Ulowetz, M. A., Marker, T. L., & Luebke, C. P. (1992). Rate based modeling of reactive distillation operations. AIChE annual meeting, Session 3, Distillation with reaction.
Pisarenko, 1993, Search for the set of stationary states of co-current reaction mass transfer processes, Theoretical Foundations of Chemical Engineering, 27, 539
Pisarenko, 1995, Infinite-efficiency operating conditions in analysis of statics of reactive rectification, Theoretical Foundations of Chemical Engineering, 29, 556
Pisarenko, 1996, Possible modes of separation in continuous reactive-distillation processes, Theoretical Foundations of Chemical Engineering, 30, 585
Pisarenko, 1997, Application of the concept of a limiting paths to estimating the feasibility of steady states in analyzing the statics of reactive-distillation processes, Theoretical Foundations of Chemical Engineering, 31, 43
Pisarenko, 1988, Conditions for a steady state in a reactive distillation operation, Theoretical Foundations of Chemical Engineering, 22, 31
Pisarenko, 1988, Dynamics of continuous evaporation with a chemical reaction, Theoretical Foundations of Chemical Engineering, 22, 483
Pisarenko, 1988, Steady states for a reactive-distillation column with one product stream, Theoretical Foundations of Chemical Engineering, 21, 281
Pisarenko, 1992, Statics of systems involving chemical conversions, Theoretical Foundations of Chemical Engineering, 25, 519
Podrebarac, 1998, The production of diacetone alcohol with catalytic distillation — Part I, Chemical Engineering Science, 53, 1067, 10.1016/S0009-2509(97)00427-2
Podrebarac, 1998, The production of diacetone alcohol with catalytic distillation — Part II, Chemical Engineering Science, 53, 1077, 10.1016/S0009-2509(97)00428-4
Powell, 1965, A method for minimizing a sum of squares of nonlinear functions without calculating derivatives, Computer Journal, 7, 303, 10.1093/comjnl/7.4.303
Quang, D. V., Amigues, P., Gaillard, J. F., Leonard, J., & Nocca, J. L. (1989). Process for manufacturing a tertiary alkyl ether by reactive distillation, US patent 4847430.
Quitain, 1999, Reactive distillation for synthesizing ethyl tert-butyl ether from bioethanol, Journal of Chemical Engineering Japan, 32, 280, 10.1252/jcej.32.280
Quitain, 1999, Industrial-scale simulation of proposed process for synthesizing ethyl tert-butyl ether from bioethanol, Journal of Chemical Engineering Japan, 32, 539, 10.1252/jcej.32.539
Rapmund, 1998, Multiple steady states in a reactive distillation column for the production of the fuel ether TAME II experimental validation, Chemical Engineering and Technology, 21, 136, 10.1002/(SICI)1521-4125(199802)21:2<136::AID-CEAT136>3.0.CO;2-4
Rascol, 1998, Numerical problems encountered in the simulation of reactive absorption: DAE index reduction and consistent initialisation, Computers and Chemical Engineering, 22, S929, 10.1016/S0098-1354(98)00183-5
Rehfinger, 1990, Kinetics of methyl-tert-butyl ether liquid-phase synthesis catalysed by ion exchange resin. I — intrinsic rate expression in liquid phase activities, Chemical Engineering Science, 45, 1605, 10.1016/0009-2509(90)80013-5
Rehfinger, 1990, Kinetics of methyl-tert-butyl ether liquid phase synthesis catalysed by ion exchange resin. II — macropore diffusion of MeOH as rate controlling step, Chemical Engineering Science, 45, 1619, 10.1016/0009-2509(90)80014-6
Reuter, 1989, Modeling of multicomponent batch distillation processes with chemical reaction and their control systems, Computers and Chemical Engineering, 13, 499, 10.1016/0098-1354(89)85032-X
Rev, 1994, Reactive distillation and kinetic azeotropy, Industrial and Engineering Chemistry Research, 33, 2147, 10.1021/ie00033a022
Roat, 1986, The integration of rigorous dynamic modeling and control system synthesis for distillation columns
Rowlinson, 1969
Ruiz, 1995, Reactive distillation dynamic simulation, Chemical Engineering Research and Design, Transactions of the Institution of Chemical Engineers, Part A, 73, 363
Saito, 1971, Separation of meta- and para-xylene mixture by distillation accompanied by chemical reactions, Journal of Chemical Engineering Japan, 4, 37, 10.1252/jcej.4.37
Sandler, 1999
Savkovic-Stevanovic, J. (1982). Mathematical model of unsteady state distillation column with association reaction. Proceedings of the third Austrian–Italian–Yugoslav Congress on chemical engineering, Graz, Austria, Vol. I (pp. 326–332).
Savkovic-Stevanovic, 1992, Reactive distillation with ion exchangers, Separation Science and Technology, 27, 613, 10.1080/01496399208018906
Sawistowski, H., & Pilavakis, P. A. (1979). Distillation with chemical reaction in a packed column. Institute of Chemical Engineers Symposium Series, 56, 4.2/49-63.
Sawistowski, 1988, Performance of esterification in a reaction-distillation column, Chemical Engineering Science, 43, 355, 10.1016/0009-2509(88)85048-6
Scenna, 1998, Dynamic simulation of startup procedures of reactive distillation columns, Computers and Chemical Engineering, 22, S719, 10.1016/S0098-1354(98)00133-1
Schenk, 1999, A hybrid modelling approach for separation systems involving distillation, Chemical Engineering Research and Design, Transactions of the Institution of Chemical Engineers, Part A, 77, 519, 10.1205/026387699526557
Schneider, 1999, Dynamic modelling of reactive absorption with the Maxwell–Stefan approach, Chemical Engineering Research and Design, Transactions of the Institution of Chemical Engineers, Part A, 77, 633, 10.1205/026387699526683
Schniep, 1945, Continuous process for acetylation of 2,3-butylene glycol, Industrial and Engineering Chemistry, 37, 872, 10.1021/ie50429a023
Schoenmakers, 1982, Possibilities of suppressing undesired reactions in distillation columns, Chemie Ingenieur Technik, 54, 1196, 10.1002/cite.330541222
Schrans, 1996, Dynamic simulation of reactive distillation. An MTBE case study, Computers and Chemical Engineering, 20, S1619, 10.1016/0098-1354(96)00275-X
Seader, 1985, The B.C. (Before Computers) and A.D. of equilibrium-stage operations, Chemical Engineering Education, 19, 88
Seader, 1998
Seider, 1996, Multiphase equilibria of reactive systems, Fluid Phase Equilibria, 123, 283, 10.1016/S0378-3812(96)90039-4
Serafimov, 1999, Optimization of reactive distillation processes, Theoretical Foundations of Chemical Engineering, 33, 455
Serafimov, 1999, Coupling chemical reaction with distillation: Thermodynamic analysis and practical applications, Chemical Engineering Science, 54, 1383, 10.1016/S0009-2509(99)00051-2
Serafimov, 1993, Reaction-mass transfer processes, Theoretical Foundations of Chemical Engineering, 27, 1
Sharma, 1985, Separations through reactions, Journal of Separation Process Technology, 6, 9
Shoemaker, 1987, Cumene by catalytic distillation, Hydrocarbon Processing, 66, 57
Siirola, J. J. (1995). An industrial perspective on process synthesis. A.I.Ch.E. Symposium Series No. 304, Vol. 91 (pp. 222–233).
Simandl, 1991, Extension of the simultaneous solution and inside–outside algorithms to distillation with chemical reactions, Computers and Chemical Engineering, 15, 337, 10.1016/0098-1354(91)80007-I
Sivasubramanian, 1990, The heat and mass transfer approach for modeling multicomponent separation processes, 331
Smith, Jr., L. A. (1984). Catalytic distillation structure, US patent 4443559.
Smith, Jr., L. A. (1985). Catalytic distillation process and catalyst, European patent 008860B1.
Smith, 1982
Sneesby, 1997, ETBE synthesis via reactive distillation. 1. Steady-state simulation and design aspects, Industrial and Engineering Chemistry Research, 36, 1855, 10.1021/ie960283x
Sneesby, 1997, ETBE synthesis via reactive distillation. 2. Dynamic simulation and control aspects, Industrial and Engineering Chemistry Research, 36, 1870, 10.1021/ie970053y
Sneesby, M. G., Tadé, M. O., & Smith, T. N. (1997c). Implications of steady-state multiplicity for operation and control of etherifcation columns. Distillation and absorption '97, Institute of the Chemical Engineers Symposium Series, 142 (pp. 205–216).
Sneesby, 1998, Detrimental influence of excessive fractionation on reactive distillation, American Institute of Chemical Engineers Journal, 44, 388, 10.1002/aic.690440215
Sneesby, 1998, Two-point control of a reactive distillation column for composition and conversion, Journal of Process Control, 9, 19, 10.1016/S0959-1524(98)00007-9
Sneesby, 1998, Mechanistic interpretation of multiplicity in hybrid reactive distillation: Physically realisable cases, Industrial and Engineering Chemistry Research, 37, 4424, 10.1021/ie970938+
Sneesby, 1998, Steady-state transitions in the reactive distillation of MTBE, Computers and Chemical Engineering, 22, 879, 10.1016/S0021-9290(97)00273-1
Sneesby, 1998, Multiplicity and pseudo-multiplicity in MTBE and ETBE reactive distillation, Chemical Engineering Research and Design, Transactions of the Institution of Chemical Engineers, Part A, 76, 525, 10.1205/026387698525009
Solokhin, 1990, Open evaporation processes accompanied by chemical reactions in the liquid phase, Theoretical Foundations of Chemical Engineering, 24, 103
Solokhin, 1990, Dynamical system for open evaporation process in presence of A=B chemical reaction, Theoretical Foundations of Chemical Engineering, 24, 377
Song, 1998, Measurement of residue curve maps heterogeneous kinetics in methyl acetate synthesis, Industrial and Engineering Chemistry Research, 37, 1917, 10.1021/ie9708790
Sørensen, 1996, Optimal control and on-line operation of reactive batch distillation, Computers and Chemical Engineering, 20, 1491, 10.1016/0098-1354(95)00234-0
Sørensen, E., & Skogestad, S. (1992). Control strategies for a combined batch reactor/batch distillation process. Proceedings of NATO ASI on batch processing systems engineering, Antalya, Turkey, May 29–June 7.
Sørensen, 1994, Control strategies for reactive batch distillation, Journal of Process Control, 4, 205, 10.1016/0959-1524(94)80042-1
Spes, 1966, Katalytische Reaktionen in Ionenaustaucherkolonnen unter Verschiebung des chemische Geleichgewichts, Chemiker Atg/Chemische Apparatur, 90, 443
Stichlmair, 1998
Stichlmair, 1999, Reactive distillation processes, Chemical Engineering and Technology, 22, 95, 10.1002/(SICI)1521-4125(199902)22:2<95::AID-CEAT95>3.0.CO;2-#
Stringaro, J. P. (1991). Reactor including a catalyst body for performing a heterogeneous reaction, European patent 433222A1.
Stringaro, J. P. (1995). Catalyzing fixed bed reactor, US patent 5470542.
Subawalla, 1999, Design guidelines for solid-catalyzed reactive distillation systems, Industrial and Engineering Chemistry Research, 38, 3696, 10.1021/ie990008l
Subawalla, 1997, Capacity and efficiency of reactive distillation bale packing, Industrial and Engineering Chemistry Research, 36, 3821, 10.1021/ie970050l
Sundmacher, K. (1995). Reaktivdestillation mit katalytischen fuellkoerperpackungen - ein neuer Process zur Herstellung der Kraftstoffkomponente MTBE. Ph.D thesis, Universität Clausthal.
Sundmacher, 1992, Importance of irreversible thermodynamics for liquid phase ion exchange catalysis, Chemical Engineering Science, 47, 2733, 10.1016/0009-2509(92)87121-6
Sundmacher, 1993, Activity evaluation of a catalytic distillation packing for MTBE production, Chemical Engineering and Technology, 16, 279, 10.1002/ceat.270160412
Sundmacher, 1994, A macrokinetic analysis of MTBE-synthesis in chemical potentials, Chemical Engineering Science, 49, 3077, 10.1016/0009-2509(94)E0119-B
Sundmacher, 1994, Multicomponent mass transfer and energy transport on different length scales in a packed reactive distillation column for heterogeneously catalysed fuel ether production, Chemical Engineering Science, 49, 4443, 10.1016/S0009-2509(05)80032-6
Sundmacher, 1995, Oscillatory vapor–liquid transport phenomena in a packed reactive distillation column for fuel ether production, Chemical Engineering Journal, 47, 219
Sundmacher, 1996, Development of a new catalytic distillation process for fuel ethers via a detailed nonequilibrium model, Chemical Engineering Science, 51, 2359, 10.1016/0009-2509(96)00092-9
Sundmacher, 1994, Classification of reactive distillation processes by dimensionless numbers, Chemical Engineering Communication, 127, 151, 10.1080/00986449408936230
Sundmacher, 1999, Multiple reactions in catalytic distillation processes for the production of the fuel oxygenates MTBE and TAME, Chemical Engineering Science, 54, 2839, 10.1016/S0009-2509(98)00520-X
Sundmacher, 1995, Mass transfer effects on kinetics of nonideal liquid phase ethyl tert-butyl ether formation, Chemical Engineering and Technology, 18, 269, 10.1002/ceat.270180408
Suzuki, 1971, Calculation of multicomponent distillation accompanied by chemical reaction, Journal of Chemical Engineering Japan, 4, 26, 10.1252/jcej.4.26
Van Swaaij, 1992, Mass transfer accompanied with complex chemical reactions in gas-liquid systems, Chemical Engineering Science, 47, 3181, 10.1016/0009-2509(92)85028-A
Takamatsu, 1984, A new simulation procedure for multistage water/hydrogen exchange column for heavy water enrichment, Journal of Chemical Engineering Japan, 17, 255, 10.1252/jcej.17.255
Taylor, 1993
Taylor, 1994, A second generation nonequilibrium model for computer simulation of multicomponent separation processes, Computers and Chemical Engineering, 18, 205, 10.1016/0098-1354(94)85009-7
Taylor, R., & Lucia, A. (1994). Modeling and analysis of multicomponent separation processes. A.I.Ch.E. Symposium Series No. 304, vol. 91 (pp. 9–18).
Terrill, 1985, Separation of closely boiling mixtures by reactive distillation 1. Theory, Industrial and Engineering Chemistry Process Design and Development, 24, 1062, 10.1021/i200031a028
Thiel, C., Rapmund, P., Sundmacher, K., Hoffmann, U., Mohl, K. D., Kienle, A., & Gilles, E. D. (1997). Intensified production of fuel ethers in reactive distillation columns — experimental validation of predicted multiple steady states. Proceedings of the first European Congress on chemical engineering — ECCE-1, May 4–7, Florence, Vol. 2 (pp. 1423–1426).
Thiel, 1997, Residue curve maps for heterogeneously catalysed reactive distillation of fuel ethers MTBE and TAME, Chemical Engineering Science, 52, 993, 10.1016/S0009-2509(96)00454-X
Thiel, 1997, Synthesis of ETBE, Chemical Engineering Journal, 66, 181, 10.1016/S1385-8947(96)03173-7
Tierney, 1982, Calculation methods for distillation systems with reaction, Chemical Engineering Communication, 16, 91, 10.1080/00986448208911088
Timofeev, 1994, Analysis of reactive systems with selective exchange of material with the ambient medium, Theoretical Foundations of Chemical Engineering, 28, 416
Timofeev, 1988, Multiple steady states in the reaction-rectification process, Theoretical Foundations of Chemical Engineering, 22, 488
Toor, 1965, Dual diffusion - reaction coupling in first order multicomponent systems, Chemical Engineering Science, 20, 941, 10.1016/0009-2509(65)80092-6
Towler, 2000, Reactive distillation
Trambouze, 1990, Countercurrent two-phase flow fixed bed catalytic reactors, Chemical Engineering Science, 45, 2269, 10.1016/0009-2509(90)80105-N
Ung, 1995, Vapor liquid phase equilibrium in systems with multiple chemical reactions, Chemical Engineering Science, 50, 23, 10.1016/0009-2509(94)00180-Y
Ung, 1995, Theory of phase equilibria in multireaction systems, Chemical Engineering Science, 50, 3201, 10.1016/0009-2509(95)00159-3
Ung, 1995, Calculation of residue curve maps for mixtures with multiple equilibrium chemical reactions, Industrial and Engineering Chemistry Research, 34, 3195, 10.1021/ie00037a003
Ung, 1995, Necessary and sufficient conditions for reactive azeotropes in multireaction mixtures, American Institute of Chemical Engineers Journal, 41, 2383, 10.1002/aic.690411105
Ung, 1995, Synthesis of reactive distillation systems with multiple equilibrium chemical reactions, Industrial and Engineering Chemistry Research, 34, 2555, 10.1021/ie00047a002
Velo, 1988, Inhibition by product in the liquid-phase hydration of iso-butene to tert-butyl alcohol — kinetics and equilibrium studies, Industrial and Engineering Chemistry Research, 27, 2224, 10.1021/ie00084a006
Venimadhavan, 1994, Effect of kinetics on residue curve maps for reactive distillation, American Institute of Chemical Engineers Journal, 40, 1814, 10.1002/aic.690401106
Venimadhavan, 1999, Bifurcation study of kinetic effects in reactive distillation, American Institute of Chemical Engineers Journal, 45, 546, 10.1002/aic.690450311
Venimadhavan, 1999, A novel distillate policy for batch reactive distillation with application to the production of butyl acetate, Industrial and Engineering Chemistry Research, 38, 714, 10.1021/ie9804273
Venkataraman, 1990, Reactive distillation using ASPEN PLUS, Chemical Engineering Progress, 86, 45
Walas, 1985
Wang, J. C., & Henke, G. E. (1966). Tridiagonal matrix for distillation. Hydrocarbon Processing, 45(8), 155–163, 45(9), 169
Wang, J. C., & Wang, Y. L. (1980). A review on the modeling and simulation of multi-stage separation processes. In W. D. Seider, & R. S. H. Mah, Foundations of computer aided chemical process design, vol. II (pp. 121–170).
Wayburn, 1987, Homotopy-continuation methods for computer aided process design, Computers and Chemical Engineering, 11, 7, 10.1016/0098-1354(87)80002-9
Wiesner, 1996, Design and optimization of a nitric acid recovery plant from nitrous waste gases, Computers and Chemical Engineering, 20, S1425, 10.1016/0098-1354(96)00244-X
Xu, 1997, Study on catalytic distillation processes, Part III. Prediction of pressure drop and holdup in catalyst bed, Chemical Engineering Research and Design, Transactions of the Institution of Chemical Engineers, Part A, 75, 625, 10.1205/026387697524155
Xu, 1999, Study on catalytic distillation processes, Part IV, Chemical Engineering Research and Design, Transactions of the Institution of Chemical Engineers, Part A, 77, 16, 10.1205/026387699525837
Xu, 1999, Modeling and simulation of a semi-batch photo reactive distillation, Chemical Engineering Science, 54, 1397, 10.1016/S0009-2509(99)00073-1
Yu, 1997, Simulation of multistage catalytic stripping with a nonequilibrium stage model, Computers and Chemical Engineering, 21, 409, 10.1016/S0098-1354(96)00010-5
Zheng, 1992, Study on catalytic distillation processes, Part I, Chemical Engineering Research and Design, Transactions of the Institution of Chemical Engineers, Part A, 70, 459
Zheng, 1992, Study on catalytic distillation processes, Part II, Chemical Engineering Research and Design, Transactions of the Institution of Chemical Engineers, Part A, 70, 465
Zhu, J., & Shen, F. (1995). The modelling and simulation of reactive distillation processes. A.I.Ch.E. Symposium Series No. 304, vol. 91 (pp. 297–300).