1925 1928 1946 1953 1964 1965 1966 1971 1975 1977 1978 1979 1980 1981 1982 1983 1984 1985 1986 1987 1988 1989 1990 1991 1992 1993 1994 1995 1996 1997 1998 1999 2000 2001 2002 2003
E.V. Murphree, "Rectifying column calculations with particular reference to n component mixtures", Ind. Eng. Chem., Vol. 17 (1925), pp. 747-750.
W.K. Lewis, K.C. Chang, "Distillation. III. The mechanism of rectification", Trans. AIChE, Vol. 21 (1928), pp. 127-138.
M. Nord, "Plate Efficiencies of Benzene - Toluene - Xylene Systems in Distillation", Trans. AIChE., Vol. 42 (1946), pp. 863-881.
H. Hausen, "The Definition of the Degree of Exchange on Rectifying Plates for Binary and Ternary Mixtures", Chemie Ingr. Tech., Vol. 25 (1953), pp. 595-597.
H.L. Toor, "Prediction of Efficiencies and Mass Transfer on a Stage with Multicomponent Systems", AIChE J., Vol. 10 (1964), pp. 545-547.
G. Standart, "Distillation. V. Generalized definition of theoretical plate or stage of contacting equipment", Chem. Eng. Sci., Vol. 20 (1965), pp. 611-622.
F. Kastenek, G.L. Standart, "Distillation Tray Efficiency", Academia, Prague (1966).
G.L. Standart, "Comparison of Murphree Efficiencies with Vaporization Efficiencies", Chem. Eng. Sci., Vol. 26 (1971), pp. 985-988.
F. Kayihan, O.C. Sandall, D.A. Mellichamp, "Simultaneous Heat and Mass Transfer in Binary Distillation. I - Theory", Chem. Eng. Sci., Vol. 30 (1975), pp. 1333-1339.
F. Kayihan, O.C. Sandall, D.A. Mellichamp, "Simultaneous Heat and Mass Transfer in Binary Distillation. II - Experiment", Chem. Eng. Sci., Vol. 32 (1977), pp. 747-754.
R. Krishna, H.F. Martinez, R. Sreedhar, G.L. Standart, "Murphree Point Efficiencies in Multicomponent Systems", Trans. I.Chem.E., Vol. 55 (1977), pp. 178-183.
R. Krishna, C.B. Panchal, "Condensation of Binary Mixtures in the Presence of an Inert Gas", Chem. Eng. Sci., Vol. 32 (1977), pp. 741-745.
A.G> Medina, N. Ashton, C. McDermott, "Murphree and Vaporization Efficiencies in Multicomponent Distillation", Chem. Eng. Sci., Vol. 33 (1978), pp. 331-339.
V.P. Maikov, A.I. Balunov, N.M. Karavaev, "Analysis of multicomponent distillation with nonequilibrium stages of separation", Dokl. Akad. Nauk SSSR, Vol. 246, No. 3 (1979), pp. 674-8 [Chem. Tech.].
M.M. Dribicka, O.C. Sandall, "Simultaneous Heat and Mass Transfer for Multicomponent Distillation in a Wetted Wall Column", Chem. Eng. Sci., Vol. 34 (1979), pp. 733-739.
M.J. Lockett, R.D. Kirkpatrick, M.S. Uddin, "Froth Regime Point Efficiency for Gas-Film Controlled Mass Transfer on a Two-dimensional Sieve Tray", Trans. I.Chem.E., Vol. 57 (1979), pp. 25-34.
A.G. Medina, N. Ashton, C. McDermott, "Hausen and Murphree Efficiencies in Binary and Multicomponent Distillation", Chem. Eng. Sci., Vol. 34 (1979), pp. 1105-1112.
R. Cornelisse, A.A.C.M. Beenackers, F.P.H. Van Beckum, W.P.M. Van Swaaij, "Numerical calculation of simultaneous mass transfer of two gases accompanied by complex reversible reactions", Chem. Eng. Sci., Vol. 35 (1980), pp. 1245-1260.
R.E. Treybal, Mass-Transfer Operations, McGraw-Hill, New York (1980).
J. Aittamaa, "Estimating Multicomponent Plate Efficiencies in Distillation", Kemia-Kemi, Vol. 8 (1981), pp. 295-300, 317.
R. Krishna, R.M. Salomo, M.A. Rahman, "Ternary Mass Transfer in A Wetted Wall Column. Significance of Diffusional Interactions Part II. Equimolar Diffusion", Trans. I.Chem.E., Vol. 59 (1981), pp. 44-53.
J.L. Bravo, J.R. Fair, "Generalized Correlation for Mass Transfer in Packed Distillation Columns", Ind. Eng. Chem. Process Des. Dev., Vol. 21 (1982), pp. 162-170.
F.J. Zuiderweg, "Sieve Trays - A View of the State of the Art", Chem. Eng. Sci., Vol. 37 (1982), pp. 1441-1464.
H. Chan, J.R. Fair, "Prediction of Point Efficiencies on Sieve Trays. 2. Multicomponent Systems", Ind. Eng. Chem. Proc. Des. Dev., Vol. 23 (1983), pp. 820-826.
H. Chan, J.R. Fair, "Prediction of Point Efficiencies on Sieve Trays. 1. Binary Systems", Ind. Eng. Chem. Proc. Des. Dev., Vol. 23 (1983), pp. 814-819.
R. Krishnamurthy, Development of a nonequilibrium stage model and its application to multicomponent separation process simulation and design, PhD. Thesis (1984).
R. Krishnamurthy, R. Taylor, "A nonequilibrium stage model of multicomponent separation processes. Part III: the influence of unequal component efficiencies in process design problems", AIChE J., Vol. 31 (1985), pp. 1973-1985.
R. Krishnamurthy, R. Taylor, "A nonequilibrium stage model of multicomponent separation processes. Part I: model description and method of solution", AIChE J., Vol. 31 (1985), pp. 449-456.
J.D. Seader, "The B. C. (before computers) and A. D. of equilibrium-stage operations", Chem. Eng. Educ., Vol. 19, No. 2 (1985), pp. 88-103.
R. Krishnamurthy, R. Taylor, "A nonequilibrium stage model of multicomponent separation processes. Part II: comparison with experiment", AIChE J., Vol. 31, No. 3 (1985), pp. 456-65.
R. Krishnamurthy, R. Taylor, "Simulation of packed distillation and absorption columns", Ind. Eng. Chem. Process Des. Dev., Vol. 24, No. 3 (1985), pp. 513-24.
H. Sardar, Development of a nonequilibrium stage model for the design and simulation of gas processing units and verification with plant data, PhD. Thesis (1985).
A. Gorak, A. Vogelpohl, "Experimental Study of Ternary Distillation in a Packed Column", Separ. Sci. & Technol., Vol. 20 (1985), pp. 33-61.
R. Krishna, "Model for Prediction of Point Efficiencies for Multicomponent Distillation", Chem. Eng. Res. Des., Vol. 63 (1985), pp. 312-322.
M.J. Lockett, "Distillation tray fundamentals" (1986).
R. Krishnamurthy, R. Taylor, "Absorber simulation and design using a nonequilibrium stage model", Can. J. Chem. Eng., Vol. 64, No. 1 (1986), pp. 96-105.
M.M. Dribika, M.W. Biddulph, "Scaling-Up Distillation Efficiencies", AIChE J., Vol. 32, No. 11, November (1986), pp. 1864-1875.
J. Powers, Azeotropic and extractive distillation calculations using a nonequilibrium stage model, MS. Thesis, Clarkson University, NY (1986).
M.S. Sivasubramanian, R. Taylor, R. Krishnamurthy, "A Nonequilibrium Stage Model of Multicomponent Separation Processes. Part IV: A Novel Approach to Packed Column Design", AIChE J., Vol. 33, No. 2 (1987), pp. 325-327.
R. Krishna, "A Unified Theory of Separation Processes Based on Irreversible Thermodynamics", Chem. Eng. Commun., Vol. 59 (1987), pp. 33-64.
A. Gorak, A. Kraslawski, A. Vogelpohl, "Simulation and Optimization of Multicomponent Distillation", Chem. Ing. Tech., Vol. 59 (1987), pp. 95-106.
T.P. Ognisty, M. Sakata, "Multicomponent Diffusion: Theory vs. Industrial Data", Chem. Eng. Prog., Vol. 83, No. 3 (1987), pp. 60-65.
M.A. Kalbassi, M.M. Dribika, M.W. Bidduplh, S. Kler, J.T. Lavin, "Sieve Tray Efficiencies in the Absence of Stagnent Zones", I. Chem. E. Symp. Ser., No. 104 (1987), pp. A511-527.
J.G. Kunesh, L.L. Lahm, T. Yanagi, "Controlled Maldistribution Studies on Random Packing at a Commercial Scale", I. Chem. E. Symp. Ser., No. 104 (1987), pp. A233-244.
J. Stichlmair, S. Ulbrich, "Liquid Channeling on Trays and the Effect on Plate Efficiency", I. Chem. E. Symp. Ser., No. 104 (1987), pp. A555-567.
H. Yoshida, "Liquid Flow over Distillation Column Plates", Chem. Eng. Comm., Vol. 51 (1987), pp. 261-275.
M.F. Powers, D.J. Vickery, A. Arehole, R. Taylor, "A Nonequilibrium Stage Model of Multicomponent Separation Processes. Part V: Computational Methods for Solving the Model equations", Comp. Chem. Engng., Vol. 12, No. 12 (1988), pp. 1229-1241.
V. Kaspar, E. Eckert, T. Vanek, M. Marek, "Mathematical modeling of absorption with chemical reaction in the liquid phase in a tray column", Collect. Czech. Chem. Commun., Vol. 53, No. 8 (1988), pp. 1688-710.
M Lao, J.P. Kingsley, R. Krishnamurthy, R. Taylor, "A Nonequilibrium Stage Model of Multicomponent Separation Processes. Part VI: Simulation of Liquid-Liquid Extraction", Comp. Chem. Comm., Vol. 86 (1989), pp. 73-89.
M.S. Sivasubramanian, J.F. Boston, "A Rate-Based Approach for Modeling Multicomponent Separation Processes", CACHI (1989).
J.D. Seader, "The Rate-Based Approach for Modeling Staged Separations", Chem. Eng. Prog., Vol. 85 (1989), pp. 41-49.
M. Prado, J.R. Fair, "Fundamental Model for the Prediction of Sieve Tray Efficiency", Ind. Eng. Chem. Res., Vol. 29, No. 6 (1990), pp. 1031-1042.
G.X. Chen, A. Afacan, C. Xu, K.T. Chuang, "Performance of Combined Mesh Packing and Sieve Tray in Distillation", Can. J. Chem. Eng., Vol. 68, June (1990), pp. 382-386.
M. Lao, Nonequilibrium models for multiphase separation processes, PhD. Thesis, Clarkson University, NY (1990).
D.L. Bennett, H.J. Grimm, "Eddy Diffusivity for Distillation Sieve Trays", AIChE J., Vol. 37, No. 4 (1991), pp. 589-596.
T.R. Carey, J.E. Hermes, G.T. Rochelle, "A model of acid gas absorption/stripping using methyldiethanolamine with added acid", Gas Sep. Purif., Vol. 5, No. 2 (1991), pp. 95-109.
P. Rajniak, R. Protus, P. Patek, "Design of industrial fractionating columns", Ropa Uhlie, Vol. 33, No. 1-2 (1991), pp. 27-30.
M. Zhao, J. Yuan, S. Qiao, "Nonequilibrium simulation for gas absorption with complex reactions in multistage column", Proc. Int. Conf. Pet. Refin. Petrochem. Process., Vol. 2 (1991), pp. 999-1006.
W. Schermuly, E. Blass, "Three-Component Mass Transfer in Liquid-Liquid Extraction with the System Glycerol-Acetone-Water Part 2: Calculation and Experimental Investigation of the Three-Component Mass Transfer in a Countercurrent Extraction Column", Chem. Eng. Technol., Vol. 14 (1991), pp. 253-263.
H.A. Kooijman, R. Taylor, "Estimation of Diffusion Coefficients in Multicomponent Liquid Systems", Ind. Eng. Chem. Res., Vol. 30, No. 6 (1991), pp. 1217-1222.
A. Zimmermann, C. Gourdon, X. Joulia, A. Gorak, C. Casamatta, "Simulation of a Multicomponent Extraction Process by a Nonequilibrium Stage Model incorporating a Drop Population Model", ESCAPE I (1992).
H.Z. Kister, Distillation Design, McGraw-Hill, New York (1992).
X. Xu, F. Shen, "Use of evaluation of the transfer rate for calculation of binary mass-transfer coefficients and modeling of multicomponent distillation", Teor. Osn. Khim. Tekhnol., Vol. 26, No. 4 (1992), pp. 486-93.
G.X Chen, K.T. Chuang, C. Chien, Y. Ye, "Mass Transfer and Hydraulics of Packed Sieve Trays", Gas Sep. Pur., Vol. 6, No. 4 (1992), pp. 207-213.
H.A. Kooijman, R. Taylor, "ChemSep - Another Software System for the simulation of Separation Processes", CACHE News, No. 35, Fall (1992), pp. 1-9.
R. Taylor, H.A. Kooijman, M.R. Woodman, Industrial Applications of a NonEquilibrium Model of Distillation and Absorption Operations, I.Chem.E. Symp. Ser., No. 128, Birmingham, UK, September (1992), pp. A415-427.
Z. Yuxiang, X. Xien, "Study on Catalytic Distillatiion Processes. Part I. Mass Transfer Characteristics in Catalist bed within the Column", Trans. I. Chem. E., Vol. 70 (1992), pp. 459-464.
Z. Yuxiang, X. Xien, "Study on Catalytic Distillatiion Processes. Quasi-Homogeneous and Rate-Based Model", Trans. I. Chem. E., Vol. 70 (1992), pp. 465-470.
R. Taylor, R. Krishna, Multicomponent Mass Transfer, John Wiley, New York (1993).
X. Xu, Y. Zheng, J. Li, W. Dong, "Process simulation for synthesis of cellosolve with catalytic distillation", Huagong Xuebao (Chin. Ed.), Vol. 44, No. 3 (1993), pp. 269-76.
S. Agarwal, R. Taylor, "Distillation Column Design Calculations Using a Nonequilibrium Model", Ind. Eng. Chem. Res., Vol. 33 (1994), pp. 2631-2636.
M.Z. Lao, R. Taylor, "Modeling Mass-Transfer in 3-Phase Distillation", Ind. Eng. Chem. Res., Vol. 33 (1994), pp. 2637-2650.
R. Taylor, H.A. Kooijman, J.S. Hung, "A 2nd Generation Nonequilibrium Model for Computer-Simulation of Multicomponent Separation Processes", Comput. Chem. Eng., Vol. 18 (1994), pp. 205-217.
G. Ovejero, R. van Grieken, L Rodriguez, J.L. Valverde, "Simulation of multicomponent distillation using a nonequilibrium stage model", Sep. Sci. Technol., Vol. 29, No. 14 (1994), pp. 1805-21.
J. Zhu, F. Shen, "Study on the non-equilibrium stage model for reactive distillation processes", Jisuanji Yu Yingyong Huaxue, Vol. 11, No. 3 (1994), pp. 167-73.
E. Eckert, M. Kubicek, "Dynamic Simulation of a Distillation Column with Multiple Liquid Phases", Comp. Chem. Eng., Vol. 19 (1995).
E.Y. Kenig, A. Gorak, "A film model based approach for simulation of multicomponent reactive separation", Chem. Eng. Process., Vol. 34 (1995), pp. 97-103.
H.A. Kooijman, R. Taylor, "A Nonequilibrium Model for Dynamic Simulation of Tray Distillation-Columns", AIChE J., Vol. 41 (1995), pp. 1852-1863.
A.B.S.H. Salem, M.S. Al-Fandery, and A.A.H.M. Al Latif, "Modeling of a Packed Column Contactor", Ind. Eng. Chem. Res., Vol. 34, No. 6 (1995), pp. 2084-93.
R. Taylor, A. Lucia, Modeling and analysis of multi component separation processes, AIChE Symp. Ser., No. Fourth International Conference on Foundations of Computer-Aided Process Design, 1994 (1995), pp. 19-28.
C. Xu, M. Zhou, Ming G. Yu, "Estimation of multicomponent mass transfer coefficients of hybrid gas-liquid separation process", Tianjin Daxue Xuebao, Vol. 28, No. 2 (1995), pp. 190-4.
L. Klemas, J.A. Bonilla, "Accurately Assess Packed-Column Efficiency", Chem. Eng. Prog., July (1995), pp. 27-44.
H.A. Kooijman, R. Taylor, "Modelling Mass Transfer in Multicomponent Distillation", Chem. Eng. J., Vol. 57, No. 2 (1995), pp. 177-188.
H.A. Kooijman, Dynamic Nonequilibrium Column Simulation, PhD. Thesis, Clarkson University, NY (1995) http://www.chemsep.org/downloads/documentation.html.
R. Taylor, H.A. Kooijman, "ChemSep Release v3.1", CACHE News, No. 41, Fall (1995), pp. 13-19.
R. Taylor, H.A. Kooijman, "Modeling Separation Processes with Nonequilibrium Models", Can. Chem. News, Vol. 47, No. 9 (1995), pp. 24-27.
H. Mori, A. Oda, T. Aragaki, Y. Kunimoto, "Packed column distillation simulatiion with a rate-based method", J. Chem. Eng. Japan., Vol. 29, No. 2 (1996), pp. 307-314.
H. Mori, A. Oda, T. Aragaki, Y. Kunimoto, "Packed column distillation simulatiion with a rate-based method", J. Chem. Eng. Japan., Vol. 29, No. 2 (1996), pp. 307-314.
3) E.F. Wijn, "The effect of downcomer layout pattern on tray efficiency", Chem. Eng. J., Vol. 63 (1996), pp. 167-180.
W. Fei, X. Wen, R. Xie, "Application of non-equilibrium stage model to liquid-liquid extraction", Tsinghua Science and Technology, Vol. 1, No. 4 (1996), pp. 332-335.
M.H. Pescarini, A.A.C. Barros, M.R. Wolf-Maciel, "Development of a software for simulating separation processes using a nonequilibrium stage model", Comput. Chem. Eng., Vol. 20, No. Suppl. A, European Symposium on Computer Aided Process Engineering--6, 1996 (1996), pp. S279-S284.
J. Qin, X. Qiao, C. Zheng, "Stimulation of fluidized catalytic reaction distillation for synthesis of methylal using nonequilibrium stage model", Nanjing Huagong Daxue Xuebao, Vol. 18, No. Zengkan (1996), pp. 1-8.
W. Qin, Y. Dai, "Calculation method of non-equilibrium stage model for mass transfer parameters of multiple components in extraction column", Jisuanji Yu Yingyong Huaxue, Vol. 13, No. 2 (1996), pp. 81-85.
X. Xu, Y. Zheng, B. Wang, "Available interphase area within a catalytic distillation column", Huagong Xuebao (Chin. Ed.), Vol. 47, No. 4 (1996), pp. 505-509.
S. Yu, A. Zhou, Q. Tan, "Simulation of multistage catalytic stripping with a nonequilibrium stage model", Computers & Chemical Engineering, Vol. 21, No. 4 (1996), pp. 409-415.
K. Klemola, J. Ilme, "Distillation Efficiencies of an Industrial-Scale i-Butane/n-Butane Fractionator", Ind. Eng. Chem. Res., Vol. 35, No. 12 (1996), pp. 4579-4586.
R.J. Kouri, J. Sohlo, "Liquid and Gas Flow Patterns in Random Packings", Chem. Eng. J., Vol. 61 (1996), pp. 95-105.
Z. Olujic, "Development of a Complete Simulation Model for Predicting the Haudraulic Separation PErformance of Distillation Columns Equipped with Structured Packings", Chem. Biochem. Eng. Q., Vol. 11, No. 1 (1997), pp. 31-46.
E.Y. Kenig, Comp. Chem. Eng., Vol. 21 (1997), pp. S355-S360.
E.Y. Kenig, U. Wiesner, A. Gorak, "Modeling of reactive absorption using the Maxwell-Stefan equations", Ind. Eng. Chem. Res., Vol. 36 (1997), pp. 4425-4434.
R. Krishna, J.A. Wesselingh, "The Maxwell-Stefan approach to mass transfer", Chem. Eng. Sci., Vol. 52 (1997), pp. 861-911.
J. Brachmann, A. Dumitru, J.A. Maruhn, H. Stoecker, W. Greiner, D.H. Rischke, "Non-equilibrium fluid-dynamics in the early stage of ultrarelativistic heavy-ion collisions", Nuclear Physics A, Vol. A619, No. 3,4 (1997), pp. 391-412.
Y. Qin, Y. Xu, C. Fang, J. Tang, "Dynamic nonequilibrium stage model of multicomponent distillation processes", Huagong Xuebao (Chinese Edition), Vol. 48, No. 2 (1997), pp. 166-174.
K. Klemola, J.K. Ilme, "Effect of Two-Pass Trays on Distillation Efficiencies", Chem. Eng. Techn., Vol. 20, No. 7, pages (1997).
K. Klemola, "Tray Efficiency Prediction of an Industrial Distillation Column", Acta Polytechnica Scandinavica - Chemical Technology Series (1997), pp. 1-95.
H. Mustafa, E. Bekassy-Molnar, "Hydrodynamic Characteristics of Nutter Valve Trays, New Correlations", Trans. I. Chem. E., Vol. 75, No. A (1997), pp. 620-624.
F. Wijn, "Does the Point Efficiency on Sieve Trays Depend on Liquid Height and Flow Regime?", I. Chem. E. Symp. Ser., No. 142 (1997), pp. 809-816.
H. Kooijman, R. Taylor, "ChemProp", CACHE News, No. 44, Spring (1997), pp. 11-13.
S. Pelkonen, A. Gorak, H.A. Kooijman, R. Taylor, Operation of a packed distillation column: Modelling and Experiments, I.Chem.E. Symp. Ser., Maastricht, NL, September (1997).
S. Pelkonen, Multicomponent Mass Transfer in Packed Distillation Columns, PhD. Thesis, Dortmund University, Germany (1997).
8) J. Li, K. Fischer, J. Gmehling, "Prediction of vapor-liquid equilibria for assymmetric systems at low and high pressures with the PSRK model", Fluid Phase Equilibria, Vol. 143 (1998), pp. 71-82.
M.A. Pacheco, G.T. Rochelle, "Rate-based modeling of reactive absorption of CO2 and H2S into aqueous methyldiethanolamine", Ind. Eng. Chem. Res., Vol. 37 (1998), pp. 4107-4117.
J.D. Seader, E.J. Henley, Separation Process Principles, John Wiley, New York (1998) http://www.che.utah.edu/~seader/.
A. Higler, R. Taylor, R. Krishna, "Modeling of a reactive separation process using a nonequilibrium stage model", Computers & Chemical Engineering, Vol. 22, No. Suppl., European Symposium on Computer Aided Process Engineering--8, 1998 (1998), pp. S111-S118.
S.C. Oh, Y.S. Oh, Y.-K. Yeo, "Simulation and Optimization of the Waste Nitric Acid Recovery Process", Industrial & Engineering Chemistry Research, Vol. 37, No. 2 (1998), pp. 697-703.
S.J. Proctor, M.W. Biddulph, K.R. Krishnamurthy, "Effect of Liquid Channeling on a 1.8-M Distillation Sieve Tray", Ind. Eng. Chem. Res., Vol. 37 (1998), pp. 2535-2540.
M. Song, F.H. Yin, K. Nandakumar, K.T. Chuang, "A Three-Dimensional Model for Simulating the Maldistribution of Liquid Flows in Random Packed Beds", Can. J. Chem. Eng., Vol. 76, April (1998), pp. 161-166.
J.G. Stichlmair, J.R. Fair, Distillation. Principles and Practice, Wiley-VCH, New York (1998) http://www.wiley-vch.de/books/tis/eng/0-471-25241-7.html.
A. Kumar, S. Hartland, "Computational strategies for sizing liquid-liquid extractors", Ind. Eng. Chem. Res., Vol. 38 (1999), pp. 1040-1056.
A. Kumar, S. Hartland, "Computational strategies for sizing liquid-liquid extractors", Ind. Eng. Chem. Res., Vol. 38 (1999), pp. 1040-1056.
M. Schenk, R. gani, D. Boggle, E.N. Pistikopoulous, "A hybrid modelling approach for separation systems", submitted to Chem. Eng. Ind. Res. (1999) (1999).
E.Y. Kenig, K. Jakobsson, P. Banik, J. Aittamaa, A. Gorak, Chem. Eng. Sci., Vol. 54 (1999), pp. 1347-1352.
R. Schneider, E.Y. Kenig, A. Gorak, "Dynamic modelling of reactive absorption with the Maxwell-Stefan approach", Trans. I.Chem.E., Vol. 77, No. A (1999), pp. 633-638.
A. Higler, R. Krishna, R. Taylor, "Nonequilibrium cell model for multicomponent (Reactive) separation processes", AIChE J., Vol. 45 (1999), pp. 2357-2370.
A. Higler, R. Krishna, R. Taylor, "Nonequilibrium cell model for packed distillation columns - The influence of maldistribution", Ind. Eng. Chem. Res., Vol. 38 (1999), pp. 3988-3999.
H. Subawalla, J.R. Fair, "Design Guidelines for Solid-Catalyzed Reactive Distillation Systems", Industrial & Engineering Chemistry Research, Vol. 38, No. 10 (1999), pp. 3696-3709.
R. Baur, A.P. Higler, R. Taylor, R. Krishna, "Comparison of Equilibrium Stage and Nonequilibrium Stage Models for Reactive Distillation", Chem. Eng. J., Vol. 3501 (1999), pp. 1-15.
R. Billet, M. Schultes, "Prediction of Mass Transfer Columns with Dumped and Arranged Packings", Trans. I. Chem. E., Vol. 77, No. A (1999), pp. 498-504.
J.C. Crause, I. Nieuwoudt, "Mass Transfer in a Short Wetted-Wall Column. 1. Pure Components", Ind. Eng. Chem. Res., Vol. 38 (1999), pp. 4928-4932.
J. Ellenberger, R. Krishna, "Counter-Current Operation of Structured Catalytically Packed Columns: Pressure Drop, Holdup and Mixing", Chem. Eng. Sci., Vol. 54 (1999), pp. 1339-1345.
C.W. Fitz, Jr, D.W. King, J.G. Kunesh, "Controlled Maldistribution Studies on Structured Packing", Trans. I. Chem. E., Vol. 77, No. A (1999), pp. 482-486.
J.S. Ghalehchian, M.J. Slater, "A Possible Approach to Improving Rotating Disc Contactor Design Accounting for Drop Breakage and Mass Transfer with Contamination", Chem. Eng. J., Vol. 75 (1999), pp. 131-144.
M. Haeberl, E. Blass, "Multicomponent Effects in Liquid-Liquid Extraction", Trans. I. Chem. E., Vol. 77, No. A, October (1999), pp. 647-655.
S. Hauan, Reactive Distillation Literature (1999).
L.U. Kreul, A. Gorak, P.I. Barton, "Dynamic Rate-Based Model for Multicomponent Batch Distillation", AIChE J., Vol. 45, No. 9, September (1999), pp. 1953-1962.
R. Krishna, J.M. Van Baten, J. Ellenberger, A.P. Higler, R. Taylor, "CFD Simulations of Sieve Tray Hydrodynamics", Trans. I. Chem. E., Vol. 77, No. A (1999), pp. 639-646.
R. Macias-Salinas, J.R Fair, "Axial Mixing in Modern Packings, Gas and Liquid Phases: I. Single-Phase Flow", AIChE J., Vol. 45, No. 2, Februrary (1999), pp. 222-239.
K. Nandakumar, Y. Shu, K.T. Chuang, "Predicting Geometrical Properties of Random Packed Beds from Computer Simulation", AIChE J., Vol. 45, No. 11 (1999), pp. 2286-2297.
I. Nieuwoudt, J.C. Crause, "Mass Transfer in a Short Wetted-Wall Column. 2. Binary Systems", Ind. Eng. Chem. Res., Vol. 38 (1999), pp. 4933-4937.
D.E. Nutter, "The MVG Tray at FRI", Trans. I. Chem. E., Vol. 77, No. A (1999), pp. 493-497.
M. Siegert, J. Stichlmair, J.-U. Repke, G. Wozny, "Dreiphasenrektifikation in Packungskolonnen", Chemi Ing. Technik, Vol. 71 (1999), pp. 819-823.
M. Siegert, J. Stichlmair, "Dreiphasenrektifikation in Packungskolonnen", Chemie Ing. Technik, Vol. 71 (1999), pp. 943-944.
J.A. Wesselingh, A.M. Bollen, "Single Particles, Bubbles and Drops", Trans. I. Chem. E., Vol. 77, No. A (1999), pp. 89-96.
N.S. Yang, Z.P. Xu, K.T. Chuang, "Determine the Number of Theoretical Plates with Commercial Simulators", Hydroc. Process., August (1999), pp. 109-116.
R. Baur, R. Taylor, R. Krishna, J.A. Copati, "Influence of mass transfer in distillation of mixtures with a distillation boundary", Chem. Eng. Res. Des. (Trans.I.Chem.E.), Vol. 77 (1999), pp. 561-565.
A.P. Higler, R. Taylor, R. Krishna, "Nonequilibrium Modelling of Reactive Distillation: Multiple steady states in MTBE synthesis", Chem. Eng. Sci., Vol. 54 (1999), pp. 1389-1395.
A.P. Higler, R. Krishna, J., Ellenberger, R. Taylor, "Counter-current operation of a structured catalytically packed bed reactor: Liquid phase mixing and mass transfer", Chem. Eng. Sci., Vol. 54 (1999), pp. 5145-5152.
A.P. Higler, R. Krishna, J., Ellenberger, R. Taylor, "Counter-current operation of a structured catalytically packed bed reactor: Liquid phase mixing and mass transfer", Chem. Eng. Sci., Vol. 54 (1999), pp. 5145-5152.
A.P. Higler, R. Krishna, J., Ellenberger, R. Taylor, "Counter-current operation of a structured catalytically packed bed reactor: Liquid phase mixing and mass transfer", Chem. Eng. Sci., Vol. 54 (1999), pp. 5145-5152.
A. Higler, Modeling Reactive Distillation, PhD. Thesis, Clarkson University, NY (1999).
P. Moritz, H. Hasse, "Fluid Dynamics in reactive distillation packing Katapak-S", Chem. Eng. Sci., Vol. 54 (1999), pp. 1367-1374.
E.Y. Kenig, F. Butzmann, L. Kucka, A. Gorak, "Comparison of numerical and analytical solutions of a multicomponent reaction-mass-transfer problem in terms of the film model", Chem. Eng. Sci., Vol. 55 (2000), pp. 1483-1496.
R. Taylor, R. Krishna, "Modelling Reactive Distillation", Chem. Eng. Sci., Vol. 55 (2000), pp. 5183-5229.
J.A. Wesselingh, R. Krishna, Mass Transfer in Multicomponent Mixtures, Delft University Press, Delft (2000).
R. Baur, A.P. Higler, R. Taylor, R. Krishna,, "Comparison of equilibrium stage and nonequilibrium stage models for reactive distillation", Chemical Engineering Journal (Lausanne), Vol. 76, No. 1 (2000), pp. 33-47.
Q.-L. Liu, J.-J. Xia, Y.-T. Wu, K-J. Bian, Z.-B. Zhang, "Several important aspects of catalytic reactive distillation. (II). Process design and mathematical simulation", Nanjing Daxue Xuebao, Ziran Kexue, Vol. 36, No. 1 (2000), pp. 104-110.
N.P. Muller, H. Segura, "An overall rate-based stage model for cross flow distillation columns", Chemical Engineering Science, Vol. 55, No. 13 (2000), pp. 2515-2528.
W.-Z. Qian, Z.-W. Wang, F. Wei, D.-F. Li, J.-R. Zhang, "Hooke-Jeeves method for producing isopropylbenzene by catalytic distillation", Shiyou Huagong, Vol. 29, No. 4 (2000), pp. 279-282.
L.N. Sridhar, C. Maldonado, A. Garcia, A. De Frias, "Analysis of single-stage nonequilibrium separation process problems", AIChE Journal, Vol. 46, No. 11 (2000), pp. 2237-2244.
L.G. Torres, F.J.D. Martins, I.D.L. Bogle, "Comparison of a reduced order model for packed separation processes and a rigorous nonequilibrium stage model", Brazilian Journal of Chemical Engineering, Vol. 17, No. 4-7 (2000), pp. 915-923.
M.M. Akbarnejad, A.A. Safekordi, S. Zarrinpashne, "A Study on the Capacity of Reactive Distillation Bale Packings: Experimental Measurements, Evaluation of the Existing Models, and Preparation of a New Model", Ind. Eng. Chem. Res., Vol. 39 (2000), pp. 3051-3058.
A.A. Alhusseini, J.C. Chen, "Transport Phenomena in Turbulent Falling Films", Ind. Eng. Chem. Res., Vol. 39 (2000), pp. 2091-2100.
V. Alopaeus, J. Aittamaa, "Appropiate Simplifications in Calculation of Mass Transfer in a Multicomponent Rate-Based Distillation Tray Model", Ind. Eng. Chem. Res., Vol. 39 (2000), pp. 4336-4345.
J.M. Van Baten, R. Krishna, "Modelling Sieve Tray Hydraulics Using Computational Fluid Dynamics", Chem. Eng. J., Vol. 77 (2000), pp. 143-151.
R. Baur, R. Taylor, R. Krishna, "Development of a Dynamic Nonequilibrium Cell Model for Reactive Distillation Tray Columns", Chem. Eng. Sci., Vol. 55 (2000), pp. 6139-6154.
B.H. Bisowarno, M.O. Tade, "Dynamic Simulation of Startup in Ethyl Tert-Butyl Ether Reactive Distillation with Input Multiplicity", Ind. Eng. Chem. Res., Vol. 39 (2000), pp. 1950-1954.
E.P. Van Elk, P.C. Borman, J.A.M. Kuipers, G.F. Versteeg, "Modelling of Gas-Liquid Reactors - Implementation of the Penetration Model in Dynamic Modelling of Gas-Liquid Processes with the Presence of a Liquid Bulk", Chem. Eng. J., Vol. 76 (2000), pp. 223-237.
M.J.W. Frank, J.A.M. Kuipers, W.P.M. Van Swaaij, "How to Use Mass Transfer Correlations for Concentrated Binary Solutions", Chem. Eng. Sci., Vol. 55 (2000), pp. 3739-3742.
R. Gani, E. Bek-Pedersen, "Simple New Algorithm for Distillation Column Design", AIChE J., Vol. 46, No. 6, June (2000), pp. 1271-1274.
J.A. Garcia, J.R. Fair, "A Fundamental Model for the Prediction of Distillation Sieve Tray Efficiency. 1. Database Development", Ind. Eng. Chem. Res., Vol. 39 (2000), pp. 1809-1817.
J.A. Garcia, J.R. Fair, "A Fundamental Model for the Prediction of Distillation Sieve Tray Efficiency. 2. Model Development and Validation", Ind. Eng. Chem. Res., Vol. 39 (2000), pp. 1818-1825.
A. Higler, R. Krishna, R. Taylor, "Nonequilibrium Modeling of Reactive Distillation: A Dusty Fluid Model for Heterogeneously Catalyzed Processes", Ind. Eng. Chem. Res., Vol. 39 (2000), pp. 1596-1607.
R. Macias-Salinas, J.R. Fair, "Axial Mixing in Modern Packings, Gas, and Liquid Phases: II. Two-Phase Flow", AIChE J., Vol. 46, No. 1, January (2000), pp. 79-91.
M. Mangold, A. Kienle, E.D. Gilles, K.D. Mohl, "Nonlinear Computation in DIVA - Methods and Applications", Chem. Eng. Sci., Vol. 55 (2000), pp. 441-454.
N.P. Mueller, H. Segura, "An Overall Rate-Based Stage Model for Cross Flow Distillation Columns", Chem. Eng. Sci., Vol. 55 (2000), pp. 2515-2528.
J.-U. Repke, G. Wozny, "A Nonequilibrium Model for Three-Phase Distillation in a Packed Column" (2000).
M. Schultes, "Influence of Liquid Maldistribution on the Mass-Transfer Efficiency of Packed Columns", Ind. Eng. Chem. Res., Vol. 39 (2000), pp. 1381-1389.
M. Siegert, J. Stichlmair, J-U. Repke, G. Wozny, "Heterogeneous Azeotropic Distillation in Packed Columns: Experimental Results", Chem. Eng. Technol., Vol. 23, No. 12 (2000), pp. 1047-1050.
G.S. Sun, F.H. Yin, A. Afacan, K. Nandakumar, K.T. Chuang, "Modelling and Simulation of Flow Maldistribution in Random Packed Columns with Gas-Liquid Countercurrent Flow", Trans. I. Chem. E., Vol. 78, No. A, April (2000), pp. 378-388.
N.S. Yang, K.T. Chuang, M. Resetarits, "A New Criterion for Modelling Distillation Column Data Using Commercial Simulators", Ind. Eng. Chem. Res., Vol. 39 (2000), pp. 3308-3313.
F. Yin, Z. Wang, A. Afacan, K. Nandakumar, K.T. Chuang, "Experimental Studies of Liquid Flow Maldistributions in Random Packed Columns", not published? (2000).
R. Baur, Modeling Reactive Distillation Dynamics, PhD. Thesis, Clarkson University, NY (2000).
E.Y. Kenig, R. Schneider, A. Gorak, "Reactive absorption: Optimal process design via optimal modelling", Chem. Eng. Sci., Vol. 56 (2001), pp. 343-350.
E.Y. Kenig, H. Baeder, A. Gorak, B. Bessling, T. Adrian, "Investigation of ethyl acetate reactive distillation process", Chem. Eng. Sci., Vol. 56 (2001), pp. 6185-6193.
R. Baur, R. Taylor, R. Krishna, "Dynamic behaviour of reactive distillation tray columns described with a nonequilibrium cell model", Chem. Eng. Sci., Vol. 56 (2001), pp. 1721-1729.
R. Baur, R. Taylor, R. Krishna, "Dynamic behaviour of reactive distillation columns described by a nonequilibrium stage model", Chem. Eng. Sci., Vol. 56 (2001), pp. 2085-2102.
M.F. Doherty, M.F. Malone, "Conceptual Design of Distillation Systems" (2001).
H.A. Kooijman, R. Taylor, The ChemSep Book, Books on Demand, Norderstedt, Germany (2001) http://www.chemsep.org/book/index.html.
B.E. Poling, J.M. Prausnitz, J.P. O'Connell, The Properties of Gases and Liquids, McGraw-Hill, New York (2001).
A. Gorak, A. Hoffmann, "Catalytic distillation in structured packings: methyl acetate synthesis", AIChE Journal, Vol. 47, No. 5 (2001), pp. 1067-1076.
W. Qian, Z. Wang, F. Wei, J. Zhang, "Simulation of catalytic distillation process for cumene synthesis", Qinghua Daxue Xuebao, Ziran Kexueban, Vol. 41, No. 12 (2001), pp. 41-43, 64.
W. Qian, Z. Wang, F. Wei, Y. Jin, J. Zhang, "Nonequilibrium-stage modeling of catalytic distillation for ethylbenzene synthesis", Huagong Xuebao (Chinese Edition), Vol. 52, No. 10 (2001), pp. 853-857.
T. Qiu, L.E. Wang, Y.-X. Wu, Z.-S. Zhao, "Effective interfacial area within catalytic distillation column", Fuzhou Daxue Xuebao, Ziran Kexueban, Vol. 29, No. 1 (2001), pp. 93-96.
P.A.M. Springer, R. Krishna, "Crossing of boundaries in ternary azeotropic distillation: Influence of interphase mass transfer", International Communications in Heat and Mass Transfer, Vol. 28, No. 3 (2001), pp. 347-356.
C. Wang, "Study on hydrolysis of methyl acetate in a catalytic distillation column", Chinese Journal of Chemical Engineering, Vol. 9, No. 4 (2001), pp. 382-387.
H.-G. Wei, W.-Y. Fei, "Nonequilibrium stage model and its application in chemical engineering separation", Shiyou Huagong, Vol. 30, No. 6 (2001), pp. 486-490.
M. Attarakih, D.A. Fara, S. Sayed, "Dynamic Modeling of a Packed-Bed Glycerol-Water Distillation Column", Ind. Eng. Chem. Res., Vol. 40 (2001), pp. 4857-4865.
R. Baur, R. Taylor, R. Krishna, "Dynamic Behavior of Reactive Distillation Columns Described by a Nonequilibrium Stage Model", Chem. Eng. Sci., Vol. 56 (2001), pp. 1-18.
V.A. Danilov, A.G. Laptev, S.V. Karpeev, A. Vogelpohl, "Modelling of Multicomponent Reactive Distillation in a Tray Column" (2001) http://www.acadjournal.com/2001/V5/part2/p1.
M. Duss, H. Meierhofer, D.E. Nutter, "Effective Interfacial Area and Liquid Holdup of Nutter Rings at High Liquid Loads", Chem. Eng. Technol., Vol. 24, No. 7 (2001), pp. 716-723.
E. Eckert, T. Vanek, "Some Aspects of Rate-Based Modelling and Simulation of Three-Phase Distillation Columns", Comp. Chem. Eng., Vol. 25 (2001), pp. 603-612.
A.B. Erasmus, I. Nieuwoudt, "Mass Transfer in Structured Packing: A Wetted-Wall Study", Ind. Eng. Chem. Res., Vol. 40 (2001), pp. 2310-2321.
I.A. Furzer, "Froth Heights on Dual-Flow Trays with Heterogenous Binary Azeotropic System and a Heterogeneous Ternary System with a Homogeneous Azeotrope", Ind. Eng. Chem. Res., Vol. 40 (2001), pp. 4951-4966.
C. Hoyme, J.J. Siirola, P.R. Bienkowski, A Study of Methyl Acetate Hydrolysis Via Reactive Distillation at Elevated Temperature and Pressure, AIChE, November (2001).
I. Iliuta, F. Larachi, "Mechanistic Model for Structured-Packing-Containing Columns: Irrigated Pressure Drop, Liquid Holdup, and Packing Fractional Wetted Area", Ind. Eng. Chem. Res., Vol. 40 (2001), pp. 5140-5146.
E.Y. Kenig, H. Baeder, A. Gorak, B. Bessling, T. Adrian, H. Schoenmakers, "Investigation of Ethyl Acetate Reactive Distillation Process", Chem. Eng. Sci., Vol. 56 (2001), pp. 6185-6193.
V. Linek, T. Moucha, F.J. Rejl, "Hydraulic and Mass Transfer Characteristics of Packings for Absorption and Distillation Columns. Rauschert-Metall-Sattel-Rings", Trans. I. Chem. E., Vol. 79, No. A, October (2001), pp. 725-732.
H. Okur, M. Bayramoglu, "The Effect of the Liquid-Phase Activity Model on the Simulation of Ethyl Acetate Production by Reactive Distillation", Ind. Eng. Chem. Res., Vol. 40 (2001), pp. 3639-3646.
Z. Olujic, A. Seibert, B. Kaibel, H. Jansen, T. Rietfort, E. Zich, Performance of New Generation of Montz High Capacity Structured Packings, AIChE Spring meeting, April 22-26 (2001).
G. Pagani, A. D'Arminio Monforte, G. Bianchi, "Transfer-Based Models Implementation in an Equation Oriented Package", Comp. Chem. Eng., Vol. 25 (2001), pp. 1493-1511.
A. Pelkonen, A. Gorak, A. Ohligschlaeger, R. Kaesemann, "Experimental Study on Multicomponent Distillation in Packed Columns", Chem. Eng. Process., Vol. 40 (2001), pp. 235-243.
D.P. Rao, C.V. Goutami, S. Jain, "A Direct Method for Incorporation of Tray-Efficiency Matrix in Simulation of Multicomponent Separation Processes", Comp. Chem. Eng., Vol. 25 (2001), pp. 1141-1152.
P. Seferlis, J. Grievink, "Optimal Design and Sensitivity Analysis of Reactive Distillation Units Using Collocation Methods", Ind. Eng. Chem. Res., Vol. 40 (2001), pp. 1673-1685.
Y. Zheng, F.T.T. Ng, G.L. Rempel, "Catalytic Distillation: A Three-Phase Nonequilibrium Model for the Simulation of the Aldol Condensation of Acetone", Ind. Eng. Chem. Res., Vol. 40 (2001), pp. 5342-5349.
R. Baur, R. Taylor, R. Krishna, "Influence of column hardware on the performance of reactive distillation columns", Catalysis Today, Vol. 66 (2001), pp. 225-232.
J. Benitez, Principles and Modern Applications of Mass Transfer Operations, John Wiley, New York (2002).
P. Gunaseelan, P.C. Wankat, "Transient pressure and flow predictions for concentrated packed absorbers using a dynamic nonequilibrium model", Ind. Eng. Chem. Res., Vol. 41 (2002), pp. 5775-5788.
P.A.M. Springer, B. Buttinger, R. Baur, R. Krishna, "Crossing of the distillation boundary in homogeneous azeotropic distillation: Influence of interphase mass transfer", Ind. Eng. Chem. Res., Vol. 41 (2002), pp. 1621-1631.
R. Baur, R. Krishna, "Hardware selection and design aspects for reactive distillation columns. A case study on synthesis of TAME", Chemical Engineering and Processing, Vol. 41, No. 5 (2002), pp. 445-462.
P.A.M. Springer, R. Baur, R. Krishna, "Influence of interphase mass transfer on the composition trajectories and crossing of boundaries in ternary azeotropic distillation", Separation and Purification Technology, Vol. 29, No. 1 (2002), pp. 1-13.
J.M. Van Baten, R. Krishna, "CFD Simulations of a Bubble Column Operating in the Homogeneous and Heterogeneous Flow Regimes", Chem. Eng. Technol., Vol. 25 (2002), pp. 1081-1086.
O. Becker, "Axiale Vermischung und Massstabvergroesserung Bei Statischen Kolonnen Fuer Die Etraktion Von Fluessigkeiten", Chemie Ing. Technik, Vol. 74 (2002), pp. 59-66.
R. Darakchiev, C. Dodev, "Gas Flow Distribution in Packed Columns", Chem. Eng. Process., Vol. 41 (2002), pp. 385-393.
K.S. Fisher, G.T. Rochelle, "Effect of Mixing on Efficiencies for Reactive Tray Contactors", AIChE J., Vol. 48, No. 11, November (2002), pp. 2537-2544.
M.C. Georgiadis, M. Schenk, E.N. Pistikopoulous, R. Gani, "The Interactions of Design, Control, and Operability in Reactive Distillation Systems", Comp. Chem. Engng., Vol. 26 (2002), pp. 735-746.
K. Jakobsson, A. Pyhalahti, S. Pakkanen, K. Keskinen, J. Aittamaa, "Modelling of a Side Reactor Configuration Combining Reaction and Distillation", Chem. Eng. Sci. (2002).
H. Kooijman, R. Taylor, ChemSep -- Yet Another Tool for Distillation Modelling, AIChE Meeting, March (2002).
R. Krishna, "Reactive Separations: More Ways to Skin a Cat", Chem. Eng. Sci. (2002).
W. Last, J. Stichlmair, "Determination of Mass Transfer Parameters by Means of Chemical Absorption", Chem. Eng. Technol., Vol. 25, No. 4 (2002), pp. 385-391.
R. Macias-Salinas, J.R. Fair, "Axial Mixing Effects in Packed Gas-Liquid Contactors", Ind. Eng. Chem. Res., Vol. 41 (2002), pp. 3429-3452.
H.R. Mortaheb, H. Kosuge, K. Asano, "Hydrodynamics and Mass Transfer in Heterogeneous Distillation with Sieve Tray Column", Chem. Eng. J., Vol. 88 (2002), pp. 59-69.
C. Noeres, A. Hoffmann, A. Gorak, "Reactive Distillation: Non-Ideal Flow Behaviour of the Liquid Phase in Structured Catalytic Packings", Chem. Eng. Sci. (2002).
Z. Olujic, Delft Model - A Comprehensive Design Tool for Currugated Sheet Structured Packings, AIChE Spring meeting, March 10-14 (2002).
J. Peng, S. Lextrait, T.F. Edgar, R.B. Eldrige, "A Comparison of Steady-State Equilibrium and Rate-Based Models for Packed Reactive Distillation Columns", Ind. Eng. Chem. Res., Vol. 41 (2002), pp. 2735-2744.
S. Piche, B.P.A. Grandjean, F. Larachi, "Reconciliation Procedure for Gas-Liquid Interfacial Area and Mass-Transfer Coefficient in Randomly Packed Towers", Ind. Eng. Chem. Res., Vol. 41 (2002), pp. 4911-4920.
V.J. Pohjola, J. Tanskanen, V. Alopaeus, "The Issue of High Flux Correction in Multicomponent Reactive and Ordinary Distillation", Chem. Eng. Sci. (2002).
F. Steyer, Z. Qi, K. Sundmacher, "Synthesis of Cyclohaxanol by Three-Phase Reactive Distillation: Influence of Kinetics on Phase Equilibria", Chem. Eng. Sci. (2002).
F.H. Yin, A. Afacan, K. Nandakumar, K.T. Chuang, "CFD Simulation and Experimental Study of Liquid Dispersion in Randomly Packed Metal Pall Rings", Trans. I. Chem. E., Vol. 80, No. A, March (2002), pp. 135-144.
H.A. Kooijman, "A Modification of the Stokes-Einstein Equation for Diffusivities in Dilute Binary Mixtures", Ind. Eng. Chem. Res., Vol. 41 (2002), pp. 3326-3328.
R. Taylor, H.A. Kooijman, A. Klamt, F. Eckert, Distillation simulation with COSMO-RS, Distilation Absorption, Baden-Baden, Germany, September-October (2002).
C. Noeres, E.Y. Kenig, A. Gorak, Chem. Eng. Process., Vol. 42 (2003), pp. 157-178.
P.A.M. Springer, R. Baur, R. Krishna, "Composition trajectories for heterogeneous azeotropic distillation in a bubble-cap tray column: Influence of mass transfer", Chem. Eng. Res. Des., Vol. 81 (2003), pp. 413-426.
K. Sundmacher, A. Kienle, Reactive Distillation. Status and Future Directions., Wiley-VCH Verlag, Weinheim (2003).
H. Arellano-Garcia, W. Martini, M. Wendt, P. Li, G. Wozny, Robust Optimization of a Reactive Distillation Process under Uncertaincy, ESCAPE 13, June (2003), pp. 551-556.
G. Bozga, G. Bumbac, V. Plescu, I. Muja, C.D. Popescu, Modelling and Simulation of Kinetics and Operation for the TAME Synthesis by Catalytic Distillation, ESCAPE 13, June (2003), pp. 575-580.
E. Y. Kenig, L. Kucka, A. Gorak, "Rigorous Modeling of Reactive Absorption Processes", Chem. Eng. Technol., Vol. 26, No. 6 (2003), pp. 631-646.
M. Kloeker, E. Kenig, A. Gorak, Experimental and Theoretical Studies of the TAME Synthesis by Reactive Distillation, ESCAPE 13, June (2003), pp. 713-718.
Z. Olujic, A.F. Seibert, B. Kaibel, H. Jansen, T. Rietfort, E. Zich, "Performance Characteristics of a New High Capacity Structured Packing", Chem. Eng. Proc., Vol. 42 (2003), pp. 55-60.
N. Poth, D. Brusis, J. Stichlmair, Rigorous Optimization of Reactive Distillation in GAMS with the Use of External Functions, ESCAPE 13, June (2003), pp. 869-874.
J.-U. Repke, O. Villian, G. Wozny, A Nonequilibrium Model for Three-Phase Distillation in a Packed Column: Modelling and Experiments, ESCAPE 13, June (2003), pp. 881-886.