[2005-2010] [2000-2005] [1995-2000] [1900-1995] Number of the articles near: 300
- F. Denes, P. Lang, G. Modla, X. Joulia.: „New double column system for heteroazeotropic batch distillation”, Chem. Eng. Sci., Available online 31 Jan. 2009
Modla G. and Lang P.: “Feasibility of new pressure swing batch distillation methods”, Chem. Eng. Sci., 63/11 pp2856-2874 (2008)
- Fang, J., Lu, J., Li, C., Liu, J., “Simulation method of batch extractive distillation” Journal of Chemical Industry and Engineering (China) 58 (5), pp. 1248-1252, (2007).
- Frits, E.R, Lelkes, Z., Fonyo, Z., Rev, E., Markot, M.Cs. „Finding limiting flows of batch extractive distsillation with interval arithmetics”, AIChE Journal, 52(9), 3100-3108. (2006)
- Gerbaud, V., Joulia, X., Rodríguez-Donis, I., Baudouin, O., Rosemain, O., Vacher, A., Castelain, P., "Residue curve map analysis applied to solvent recovery by batch distillation processes", Chem. Eng. Proc., 45, 672 (2006).
- HUA Chao, LI Xingang, XU Shimin and BAI Peng, „Design and Operation of Batch Extractive Distillation with Two Reboilers”, Chin. J. Chem. Eng., 15 (2) 286-290, (2007).
- Kotai B., P. Lang, T. Balazs: „Separation of Maximum Azeotropes in a Middle Vessel Column”, IChemE Symposium Series, No. 152, 699-708, ISBN-10 0 85295 505 7, ISBN-13 978 0 85295 505 5 UK (2006).
- Kotai B., P. Lang and G. Modla, „Batch extractive distillation as a hybrid process: Separation of minimum boiling azeotropes”, Chem. Eng. Sci., 62, 23, p6816-6826, (2007)
- Lang P., Gy. Kovacs, B. Kotai, J. Gaal-Szilagyi, G. Modla, “Industrial application of a new batch extractive distillation operational policy”, Institution of Chemical Engineers, Symposium series , 152, 699-708, ISBN-10-0-85295-505-7, (2006).
- Lang P., G. Modla: „Generalised method for the determination of heterogeneous batch distillation regions”, Chem. Eng. Sci., 61, 4262-4270 (2006).
- Lechoslaw J. Krolikowski, “Determination of distillation regions for non-ideal ternary mixtures”, AIChE Journal, 52, 532-544, (2006)
- Modla G., Lang P., „New column configurations for pressure swing batch destillation I. Feasibility Studies”, DYCOPS (2007), Preprints Vol2, 105-110 (2007).
- Modla G., Lang P., „New column configurations for pressure swing batch destillation II. Rigorous simulation calculations”, DYCOPS (2007). Preprints Vol2, 361-366 (2007).
- Modla G., Lang P.,“New method for determination of batch heteroazeoropic distillation regions”, Institution of Chemical Engineers, Symposium series , 152, 440-449, ISBN-10-0-85295-505-7, (2006).
- Pommier S., Massebeuf S., Kotai B., Lang P., Baudouin O. and Floquet P., Gerbaud V., “Heterogeneous Batch Distillation Processes:Real System Optimisation”, Chemical Engineering and Processing, 47, 408–419, (2008).
- Rodríguez-Donis, I., Acosta-Esquijarosa I., Gerbaud V., Pardillo-Fondevila E., Joulia, X., „Separation of n hexane – ethyl acetate mixture by azeotropic batch distillation with heterogeneous entrainers”. Chemical Engineering and Processing. 44, 131-137. (2005).
- Rodriguez-Donis, I., Papp, K., Gerbaud, V., Joulia, X., Rev, E., & Lelkes, Z., "Column Configurations of Continuous Heterogeneous Extractive Distillation". AIChE Journal. In Press, Accepted Manuscript available online, (2007).
- Row, K.H., & Jin, Y., „Recovery of catechin compounds from Korean tea by solvent extraction”. Bioresource Technology, 97(5), 790-793. (2006).
- Skouras S., V. Kiva and S. Skogestad, “Feasible separations and entrainer selection rules for heteroazeotropic batch distillation”, Chemical Engineering Science, 60, 2895. (2005).
- Skouras S., S. Skogestad and V. Kiva, “Analysis and Control of Heteroazeotropic Batch Distillation”, AIChE Journal, 51 (4), 1144-1157. (2005).
- Steger, C., Rev, E., Horvath, L., Fonyo, Z., Meyer, M., Lelkes, Z, “New extractive configuration separating azeotropic mixture in semi-batch way” Separation and Purification Technology 52 (2), pp. 343-356 (2006).
- Steger, C., Varga, V., Horvath, L., Rev, E., Fonyo, Z., Meyer, M., & Lelkes, Z., „Feasibility of extractive distillation process variants in batch colonne de rectification column”, Chemical Engineering & Processing, 44, 1237-1256. (2005).
- Van Kaam, R., Rodriguez-Donis, I., Labrada-Fernandez, Y., Acosta-Esquijarosa, J., & Gerbaud, V., „Synthesis of non-conventional distillation processes for the separation of chloroform – methanol mixture”., Revista Cubana de Química. ISBN 959-282-27-X. (2006).
- Xu, S. L. and H. Y. Wand, “Separation of tert-butyl alcohol-water mixtures by a heterogeneous azeotropic batch distillation process”, Chem. Eng. Tech., 29, 113 (2006).
- Acosta, J., Arce, A., Rodil E., Soto, A., "A thermodynamic study on binary and ternary mixtures of acetonitrile, water and butyl acetate, Fluid Phase Equilibria", 203, 83 (2002).
- Brüggemann, S., & Marquardt, W. „Shortcut methods for nonideal multicomponent distillation: 3. Extractive distillation columns.” AIChE Journal, 50, 1129-1149. (2004).
- Chemstations, ”CHEMCAD User Guide”, Chemstation, (2000).
- Cui XB, Yang ZC, Zhai YR, et al., „Batch extractive distillation in a column with a middle vessel”, Chinese J Chem Eng 10 (5), 529-534 (2002).
- Chien, I. L., K. L. Zeng, H. Y. Chao, and J. H. Liu, “Design and control of acetic acid dehydration system via heterogeneous azeotropic distillation,” Chemical Engineering Science, 59, 4547 (2004).
- Doherty, M. F., & Malone, M. F. „Conceptual design of distillation systems (1st ed.)”, New York: McGraw-Hill. (2001).
- Fernhloz G., S. Engells, L.U. Kreul, A. Gorak, „Optimal operation of a semi-batch reactive distillation column”, Comp. Chem. Eng. 24, (2–7), 1569–1575, (2000).
- Fraga E.S., A. Zilinskas, „Evaluation of hybrid optimization methods for the optimal design of heat integrated distillation sequences”, Adv. Eng. Softw. 34 (2) 73–86. (2003).
- Hilmen Eva-Katrine, ”Separation of Azeotropic Mixtures:Tools for Analysis and Studies on Batch Distillation Operation”, Thesis, Norwegian University of Science and Technology Departmant of Chemical Engineering, (2000).
- Hilmen, E. K., Kiva, V. N., & Skogestad, S. „Topology of ternary VLE diagrams: elementary cells”. AIChE Journal, 48(4), 752–759. (2002).
- Hanke M., P. Li, „Simulated annealing for the optimization of batch distillation processes”, Comp. Chem. Eng. 24 11–18. (2000).
- Hilmen, E.K., Kiva, V.N., Skogestad, S., "Topology of ternary VLE diagrams: elementary cells" A.I.Ch.E. Journal 48, 4, 752 (2002).
- Kiva V.N., Hilmen E.K., Skogestad S., "Azeotropic phase equilibrium diagrams: a survey", Chem. Eng. Sci., 58, 1903 (2003).
- Kim, K., and U. M. Diwekar, ‘‘Comparing Batch Column Configurations: Parametric Study Involving Multiple Objectives,’’ AIChE J., 46, 2475 (2000).
- Kim K.J, U.M. Diwekar, „New Era in Batch Distillation: Computer Aided Analysis, Optimal Design and Control”, Rev. Chem. Eng., 17, 111 (2001).
- Láng P., “Szakaszos extraktív desztilláció”, Akadémiai értekezés, (2003).
- Lang P., G. Modla, B. Kotai, ”Batch Heteroazeotropic Rectification under Continuous Entrainer Feeding: II. Rigorous Simulation Results”, PSE2003 Computer Aided Chemical Engineering, 15, 906-909, (2004).
- Lang P., Modla G., Moszkovicz P., Kotai B., ”Homoazeotropic Distillation of Maximum Azeotropes in a Batch Rectifier with Continuous Entrainer Feeding: II. Rigorous Simulation Results”, Comp. Chem. Eng., 24, 1429, (2000b).
- Lang P., Modla, G., Benadda, B., Lelkes, Z., ”Homoazeotropic Distillation of Maximum Azeotropes in a Batch Rectifier with Continuous Entrainer Feeding: I. Feasibility Studies”, Comp. Chem. Eng., 24, 1465, (2000a).
- Lee, J. W., J. Oldenburg, S. Br¨uggemann, and W. Marquardt, ‘‘Feasibility of Batch-Reactive Distillation,’’ AIChE Meeting, Reno, NV (2001).
- Lelkes Z., Rev E., Steger C., Fonyo Z., „Separation of maximum boiling binary azeotrope in batch extractive rectifier with intermediate boiling entrainer”, AIChE J., 48, 2524, (2002).
- Modla G., P. Lang, B. Kotai and K. Molnar, ”Batch Heteroazeotropic Rectification of a Low Relative Volatility Mixture under Continuous Entrainer Feeding”, AICHE J., 49., 2533-2552 (2003).
- Modla G., P. Lang, B. Kotai and K. Molnar, ”Batch Heteroazeotropic Rectification under Continuous Entrainer Feeding: I. Feasibility Studies”, PSE2003 Computer Aided Chemical Engineering, 15, 974-977, (2004).
- Modla G., P. Lang, K. Molnar, ”Batch Heteroazeotropic Rectification of a Low Relative Volatility Mixture under Continuous Entrainer Feeding”, 6-th World Congress of Chemical Engineering, Melbourne, Australia, (2001).
- Mukherjee S., R.K. Dahule, S.S. Tambe, D.D. Ravetkar, B.D. Kulkarni, „Consider genetic algorithms to optimize batch distillation”, Hydrocarbon Process. 80 (9) 59–66. (2001).
- Noda M., A. Kato, T. Chida, S. Hasebe, I. Hashimoto, „Optimal structure and on-line optimal operation of batch distillation column”, Comp. Chem. Eng. 25 (1) 109–117. (2001).
- Noeres, C., Kenig, E. Y., Górak, A., "Modelling of reactive separation processes: reactive absorption and reactive distillation", Chem. Eng. Proc., 42, 3, 157 (2003).
- Phimister, J. R., and W. D. Seider, ‘‘Semicontinuous, Middle-Vessel Distillation of Ternary Mixtures,’’ AIChE J., 46, 1508 (2000).
- Rev E., Lelkes Z., Varga V., Steger C., Fonyo Z., ”Seperation of a minimum-boiling azeotrope in a batch extractive rectifier with an intermediate boiling entrainer”, Ind. Eng. Chem. Res., 42, 162, (2003).
- Rodríguez-Donis I., A. J. Esquijarosa, V. Gerbaud, and X. Joulia, ”Separation of minimum boiling azeotropoc mixtures by extractive batch distillation processes with heterogenous entrainers”, AIChE J., 49, 3074-3083, (2003).
- Rodríguez-Donis I., E. Pardillo-Fontdevila, V. Gerbaud, and X. Joulia, ”Synthesis, experiments and simulation of heterogeneous batch distillation processes”, Comp. Chem. Eng. 4-6, 799, (2001a).
- Rodríguez-Donis I., V. Gerbaud, and X. Joulia, ”Entrainer Selection Rules for the Separation of Azeotropic and Close Boiling Temperatures by Heterogenous Batch Distillation”, Ind. Chem. Eng. Res., 40, 4935-4950, (2001b).
- Rodríguez-Donis I., V. Gerbaud, and X. Joulia, ”Feasibility of Heterogenous Batch Distillation”, AIChE J., 48, 1168-1178, (2002).
- Ruiz Ahon, V., and J. L. de Medeiros, “Optimal Programming of Ideal and Extractive Batch Distillation: Single Vessel Operations,” Comput. Chem. Eng., 25, 1115 (2001).
- Thery, R., Llovell, F., Meyer, X., Gerbaud ,V., & Joulia, X.. "Modelling of a dynamic multiphase flash: the positive flash. Application to the calculation of ternary diagrams". Computer & Chemical Engineering, 28(12), 2469-2480. (2004).
- Zhe Guo, Mudassir Ghufran, and Jae W. Lee, "Feasible Products in Batch Reactive Distillation", AIChE J.l, 49,12, (2003)
- Ahmad, B. S., and P. I. Barton, ‘‘Homogeneous Multicomponent Azeotropic Batch Distillation,’’ AIChE J., 42, 3419 (1996).
- Ahmad B. S., Zhang Y., Barton B.I., ”Product Sequences in Azeotropic Batch Distillation”, AIChE, 44, 1051, (1998).
- Barolo, M., G. B. Guarise, S. A. Rienzi, A. Trotta, ”Understanding The Dynamics of a Batch Distillation Column with a Middle Vessel”, Comp. chem. Engng. 22, S37 (1998).
- Betlem B.H.L., H.C. Krinjsen, H. Huijnen, „Optimal batch distillation control based on specific measures”, Chem. Eng. J. 71 (2) 111–126, (1998).
- Biegler, L. T., Grossmann, I. E., & Westerberg, A. W. „Systematic methods of chemical process design”. Englewood CliIs, NJ: Prentice-Hall. (1997).
- Bonny, L., ‘‘Multicomponent Batch Distillations: Study of Operating Parameters,’’ Ind. Eng. Chem. Res., 38, 4759 (1999).
- Bonny L., P. Floquet, S. Domenech, L. Pibouleau, „Optimal strategies for batch distillation campaign of different mixtures”, Chem. Eng. Process., 35 349–361. (1996).
- Bonny L., P. Floquet, S. Domenech, L. Pibouleau, „Strategies for slop cut recycling in multicomponent batch distillation”, Chem. Eng. Process. 33 (1) 23–31. (1994).
- Cheong W., Barton P., "Azeotropic distillation in a middle vessel batch column. 1. Model formulation and linear separation boundaries", Ind. Eng. Chem. Res., 38 1504 (1999a).
- Cheong W., Barton P., "Azeotropic distillation in a middle vessel batch column. 2. Model validation", Ind. Eng. Chem. Res., 38, 1549 (1999b).
- Cheong W., Barton P., "Azeotropic distillation in a middle vessel batch column. 3. Nonlinear separation boundaries", Ind. Eng. Chem. Res., 38, 1531 (1999c).
- Chien I-L., C.J. Wang and D. S. H. Wong, ””, Ind. Chem. Eng. Res., 38, (1999).
- Chien I-L., C.J. Wang et al., ”Experimental Investibation of Optimal Conventional Control Strategy for a Heterogeneous Azeotropic Distillation Column”, Comp. Chem. Eng., S249-252, (1999).
- Düssel R., J. Stichlmair, ”Separation of Azeotropic Mixtures by Batch Distillation Using an Entrainer”, Comp. Chem. Eng. 19, 113-118, (1995).
- Farhat S., L. Pibouleau, P. Floquet, S. Domenech, „Politiques de Taux de Reflux Optimal pour la Distillation Discontinue deM´elanges Binaires”, R´ec. Prog. G´en. Proc., 3 (9), 435–440, (1989).
- Fonyó Zs., Fábry Gy., ”Vegyipari muvelettani alapismeretek”, Nemzeti Tankönyvkiadó, Budapest, 597 (1998).
- Fraga E.S., T.R.S. Matias, „Synthesis and optimization of a non-ideal distillation system using a parallel genetic algorithm”, Comp. Chem. Eng. 20S, S79–S84. (1996).
- Frey T., M.H. Bauer, J. Stichlmair, „MINLP-optimization of complex column configurations for azeotropic mixtures”, Comp. Chem. Eng. 21S, S217–S222, (1997).
- Furlonge, H. I., C. C. Pantelides, and E. Spensen, “Optimal Operation of Multivessel Batch Distillation Columns,” AIChE J., 45, 781, (1999).
- Hasabe, S., M. Noda, and I. Hashimoto, ‘‘Optimal Operation Policy for Multi-Effect Batch Distillation System,’’ Comput. Chem. Eng., 21, S1221 (1997).
- Kao C., „Performance of several non-linear programming software packages on microcomputers”, Comput. Oper. Res. 25 (10) 807–816. (1998)
- Kim Y.H., „Optimal design and operation of a multi-product batch distillation column using dynamic model”, Chem. Eng. Process. 38 (1) 61–72. (1999).
- Lang, P., Lelkes Z., Otterbein M., Benadda B., Modla G. ”Feasibility studies for batch extractive distillation with a light entrainer”, Comp. Chem. Eng., 23, S93-S96, (1999).
- Lee, F.M. „Extractive Distillation: Separating Close – Boiling – Point Mixtures”, Chemical Engineering, 105(12), 112-121. (1998).
- Lelkes Z., Lang P., Moszkovicz P., Benadda B., Otterbein M., „Batch extractive distillation: the process and the operational policies”, Chem. Eng. Sci., 53,1331, (1998a).
- Lelkes Z., Lang P.,. Benadda B., Moszkovicz P., ”Feasibility of Extractive Distillation in a Batch Rectifier”, AIChE J., 44, 810, (1998b).
- Lelkes, Z., Lang P., Otterbein M., ”Feasibility and Sequencing for Homoazeotropic Distillation in a Batch Rectifier with Continuous Entrainer Feeding”, Comp. Chem. Eng., 22, S653-S656, (1998c).
- Lotter, S. P., and U. M. Diwekar, ‘‘Shortcut Models and Feasibility Considerations for Emerging Batch Distillation Columns,’’ Ind. Eng. Chem. Res., 36, 760 (1997).
- Milani, S. M., “Optimization of Solvent Feed Rate for Maximum Recovery of High Purity Top Product in Batch Extractive Distillation,” Trans. Inst. Chem. Eng., 77, 469 (1999).
- Muller D. and Marquardt, W.,””, Ind. Chem. Eng. Res., 36, 5410, (1997).
- Mutjaba I.M., S. Macchietto, „Simultaneous optimization of design and operation of multicomponent batch distillation column—single and multiple separation duties”, J. Process Contr. 6 (1) 27–36. (1996).
- Mujtaba, I. M., “Optimization of Batch Extractive Distillation Processes for Separating Close Boiling and Azeotropic Mixtures,” Trans. Inst. Chem. Eng., 77, 588 (1999).
- Novak Z., Z. Kravanja, I.E. Grossmann, „Simultaneous synthesis of distillation sequences in overall process schemes using an improved MINLP approach”, Comp. Chem. Eng. 20, (12), 1425–1440. (1996).
- Peterson E.J., Partin L.R., "Temperature sequences for categorising all ternary distillation boundary maps", Ind. Chem. Eng. Res., 36, 1799 (1997).
PPollmann, P., Bauer, M. H., & Blass, E. „Investigation of vapour–liquid equilibrium of non-ideal multicomponent systems”, Gas Separation and Purification, 10(4), 225–241. (1996).
- Rooks, R. E., Julka, V., Doherty, M. F., & Malone, M. F. „Structure of distillation regions for multicomponent azeotropic mixtures”, A.I.Ch.E. Journal, 44(6), 1382–1391, (1998).
- Rovaglio M., T. Faravelli, P. Gaffuri, C. Di Palo, A. Dorigo, ”Controllability and Operability of Azeotropic Heterogeneous Distillation Systems”, Comp. Chem. Eng., 19, S525-S530, (1995).
- Safrit, B. T. „Synthesis of azeotropic batch distillation separation systems”, Ph.D. thesis, Carnegie Mellon University, Pittsburgh, USA. (1996).
- Safrit, B. T., A. W. Westerberg, U. Diwekar, and O. M. Wahnschafft, ‘‘Extending Continuous Conventional and Extractive Distillation Feasibility Insights to Batch Distillation,’’ Ind. Eng. Chem. Res., 34, 3257 (1995).
- Safrit, B. T., & Westerberg, A. W. „Algorithm for generating the distillation regions for azeotropic multicomponent mixtures”, Industrial and Engineering Chemistry Research, 36, 1827–1840. (1997).
- Safrit, B. T., and A. W. Westerberg, ‘‘Improved Operational Policies for Batch Extractive Distillation Columns,’’ Ind. Eng. Chem. Res., 36, 436 (1997).
- Seader, J. D., & Henley, E. J. „Separation process principles”, New York: Wiley. (1998).
- Serafimov, L. A. „Thermodynamic and topological analysis of liquid–vapor phase equilibrium diagrams and problems of rectification of multicomponent mixtures”. In S. I. Kuchanov (Ed.), Mathematical methods in contemporary chemistry (pp. 557–605). Amsterdam: Gordon and Breach Publishers. (1996).
- Serafimov, L. A., Kushner, T. M., & Cheluskina, T. V. „Thermodynamic-topological analysis of VLE diagrams for ternary mixtures with two ternary azeotropes. In Papers collection: Problems of thermodynamics of heterogeneous systems and the theory of interfacial effects”, Issue 10, St. Petersburg University, St. Petersburg, pp. 26–55. (1996).
- Sorensen E., S. Skogestad, „Comparison of regular and inverted batch distillation”, Chem. Eng. Sci. 51, (22), 4949–4962. (1996).
- Sorensen, E., ‘‘A Cyclic Operation Policy for Batch DistillationTheory and Practice,’’ Comput. Chem. Eng., 23, 533 (1999).
- Spellucci P., „An SQP method for general non-linear programs using only equality constraints subproblems”, Math. Program. 82 413–448. (1998).
- Tolsma J. E., P. Barton, ”Computation of heteroazeotropes”, Comp.Chem. Engng., 22, S61, (1998).
- Tomazi, K. G., “Limitations and Dynamics Imposed on Multicomponent Batch Distillation by Tray Hydraulics,” Ind. Eng. Chem. Res., 36, 4273 (1997).
- Venimadhavan, G., M. F. Malone, and M. F. Doherty, ‘‘A Novel Distillation Policy for batch reactive Distillation with Application to the Production of Butyl Acetate,’’ Ind. Eng. Chem. Res., 38, 714 (1999).
- Warter, M., and J. Stichlmair, “Batchwise Extractive Distillation in a Column with a Middle Vessel,” Comput. Chem. Eng. Suppl., S23, S91S (1999).
- Watson S., Xavier Julia et al., ”Azeotropic Batch Distillation”, Comp. Chem. Eng. 19, 589-596, (1995).
- Widagdo S. and W.D. Seider, „Azeotropic Distillation”, AIChe J., 42, 96, (1996).
- Wittgens B., S. Skogestad, „Closed Operation of Multivessel Batch Distillation: Experimental Verification”, AIChE Journal, 46, 1209 (2000).
- Babich, S. V. „Development of the separation technology for light fraction of the gasoline oxidate by means of thermodynamic-topological analysis”. Ph.D. thesis, Lomonosov Institute of Fine Chemical Technology, Moscow, Russia (in Russian). (1972).
- Baburina, L. V., Platonov, V. M., & Slinko, M. G. „Thermodynamic investigation of phase diagrams of ternary azeotropic mixtures”. Doklady Akademii nauk SSSR, 269(1), 129–133 (in Russian). (1983).
- Baburina, L. V., Platonov, V. M., & Slinko, M. G. „Classification of vapor–liquid equilibrium diagrams for homogeneous azeotropic mixtures”. Theoretical Foundations in Chemical Engineering, 22(4), 390–396 [535–542]. (1988).
- Benedict M., Rubin L. C., “Extractive and Azeotropic Distillation. I. Theoretical Aspects”, Trans. Am. Inst. Chem. Eng., 41, 153, (1945).
- Berg, L. „Azeotropic and extractive distillation: Selecting the agent for distillation”, Chemical Engineering Progress, 65, 52-57. (1969).
- Bernot, C. „Design and synthesis of multicomponent batch distillation”. Ph.D. thesis. University of Massachusetts, Amherst, USA. (1990).
- Bernot Ch., M. Doherty and M. F. Malone, “Design and Operating Targets for Nonideal Multicomponent Batch Distillation”, Ind. Eng. Chem. Res. 32, 293, (1993).
- Bernot Ch., M. Doherty, M. F. Malone, ”Feasibility and Separation Sequencing in Multicomponent Batch Distillation”, Chem. Eng. Sci., 46, 1311, (1991).
- Bernot Ch., M. Doherty, M. F. Malone, “Patterns of Composition Change in Multicomponent Batch Distillation”, Chem. Eng. Sci., 45, 1207, (1990).
- Bogdanov, V. S., & Kiva, V. N. „Localization of single [Unity] K- and -lines in analysis of liquid–vapor phase diagrams”, Russian Journal of Physical Chemistry, 51(6), 796–798, [1349–1352]. (1977).
- Bortolini, P., G. B. Guarise, „Un nuovo methodo di distillazione discontinua” , Quad. Ing. Chim. Ital., 6 (9), 150 (1970).
- Bossen, B.S., Jorgensen, S.B., & Gani, R, „Simulation, design and analysis of azeotropic distillation Oderations", Ind. & Eng. Chem.Res., 32, 620-633. (1993).
- Boyarinov, A. I., Vetokhin, V. N., Gartman, T. N., Kafarov, V. V., & Motyl’, D. N. „Calculation of the limits of distillation regions [Calculation of residue curve boundaries]”. Russian Journal of Physical Chemistry, 48(2), 299–302. (1974).
- Bushmakin, I. N., & Kish, I. „Isobaric liquid–vapor equilibrium in a ternary system with an azeotrope of the saddlepoint type”. Russian Journal of Applied Chemistry, 30(2), 205–215 [200–211]. (1957).
- Bushmakin, I. N., & Molodenko, P. Ya. „The choice of entrainer for azeotropic rectification”. Vestnik of Leningrad State University, Series Physics and Chemistry, 10, 68–92 (in Russian). (1957).
- Bril Zs. A., Mozzsuhin A. C., Petljuk F. B., Serafimov L. A., “Mathematical modelling of the rectification of multicomponent mixtures with liquid phase splitting on the plates of the column”, Teor. Osn. Chim. Technol., 8, 351, (1974).
- Bushmakin I.N., and Molodenko P.Ya, ”The Choice of Entrainer for Azeotropic Rectification”, Vestnik of Leningrad State University, Ser. Physics and Chemistry 10, 68-91, (1957).
- Chu, J.C., Getty, R.L., Brennecke, L.F., Paul, R., "Distillation equilibrium data", Reinhold, New York (1950).
- Chu, J.C., Wang, S.L., Levy, S.L., and Paul, R., "Vapor-liquide equilibrium data", Edwards, Ann Arbor, MI (1956).
- Coulson J. M., J. F. Richardson, ”Chemical Engineering”, 3rd edition, Vol. 2, 478, Pergamon Press, Oxford (1978).
- Coward I., „The time-optimal problem in binary batch distillation”, Chem. Eng. Sci., 22 (4) 503–516., (1967)
- Davidyan, A. G., V. N. Kiva, G. A. Meski, and M. Morari, ‘‘Batch Distillation in a Column with a Middle Vessel,’’ Chem. Eng. Sci., 49, 3033 (1994).
- Distefano G. P., "Mathematical Modeling and Numerical Integration of Multicomponent Batch Distillation Equations", AIChE J., 14, 190 (1968).
- Diwekar U. M., Madhavan K. P., ”Multicomponent Batch Distillation Column Design”, Ind. Eng. Chem. Res., 30, 713 (1991).
- Doherty M. F. and Glenn A. Caldarola, ”Design and Synthesis of Homogeneous Azeotropic Distillations 3. The Sequencing of Columns for Azeotropic and Extractive Distillations”, Ind. Eng. Chem. Fundam. 24, 474-485, (1985).
- Doherty M. F., J. D. Perkins, ”On the dynamics of distillation process-I”, Chem. Eng. Sci. 33, 281-301, (1978a).
- Doherty M. F., J. D. Perkins, ”On the dynamics of distillation process-II”, Chem. Eng. Sci. 33, 569-573, (1978b).
- Doherty M. F., J. D. Perkins, ”On the dynamics of distillation process-III”, Chem. Eng. Sci. 34, 1401, (1979a).
- Doherty M. F., J. D. Perkins, ”The Behaviour of Multicomponent Azeotropic Distillation Processes”, Inst. Chem. E. Symp. Ser. 56, 21-48, (1979b).
- Doherty M.F., Perkins J.D., "On the dynamics of distillation processes - IV. Uniqueness and stability of the steady state in homogeneous continuous distillations", Chem. Eng. Sci., 37, 381 (1982).
- Doherty, M.F., Caldarola, G.A., "Design and synthesis of homogeneous azeotropic distillation - III. The sequencing of columns for azeotropic and extractive distillations", Ind. Eng. Chem. Fundam., 24, 474 (1985).
- Doherty, M. F. „The presynthesis problem for homogeneous azeotropic distillation has a unique explicit solution”. Chemical Engineering Science, 40(10), 1885–1889. (1985).
- Doherty, M. F., & Knapp, J. F., „Distillation, Azeotropic and Extractive (Vol. 8)” (4th ed.), Kirk-Othmer Encyclopedia of Chemical Technology. (1993).
- Ewell, R. H., & Welch, L. M.. „Rectification in ternary systems containing binary azeotropes”, Industrial and Engineering Chemistry Research, 37(12), 1224–1231. (1945).
- Farhat S., M. Czernicki, L. Pibouleau, S. Domenech, „Optimization of multiple-fraction batch distillation by non-linear programming”, AIChE J. 36 (9), 1349–1360., (1990).
- Fidkowski Z. T., M. F. Doherty, M. F. Malone, ”Feasibility of Separations Distillation of Nonideal Ternary Mixtures”, AIChE J., 39, 1303 (1993a).
- Fidkowski Z. T., M. F. Malone, M. F. Doherty, ”Nonideal Multicomponent Distillation: Use of Bifurcation Theory for Design”, AIChE J., 37, 1761 (1991).
- Fidkowski Z. T., M. F. Malone, M. F. Doherty. „Computing azeotropes in multicomponent mixtures”, Comput. Chem. Eng., 17, 1141 (1993b).
- Fien, G. -J. A. F., & Liu, Y. A. „Heuristic synthesis and shortcut design of separation processes using residue curve maps: A review”. Industrial and Engineering Research, 33, 2505–2522. (1994).
- Foucher, E. R., Doherty, M. F., & Malone, M. F. „Automatic screening of entrainers for homogeneous azeotropic distillation”, Industrial and Engineering Chemistry Research, 30, 760–772., (1991).
- Gmehling, J., and U. Onken, "Vapour-Liquid Equilibrium Data Collection, Chemistry Data Series", DECHEMA, Frankfurt (1977).
- Gmehling J., J. Menke, J. Krafczyk and K. Fishher, ”Azeotropic Data I-II”, VCH-Publishers, Weinheim, New York (1994).
- Gurikov, Y. V. „Structure of the vapor–liquid equilibrium diagrams of ternary homogeneous solutions”. Russian Journal of Physical Chemistry, 32(9), 1980–1996 (abstract in English) (in Russian). (1958).
- Hasabe, H., B. B. A. Aziz, I. Hashimoto, and T. Watanabe, ‘‘Optimal Design and Operation of Complex Batch Distillation Column,’’ Proc. IFAC Workshop, London, p. 177 (1992).
- Horsley L. H., ”Azeotropic Data I-II”, American Chemical Society, Washington, (1973).
- Horsley L. H., ”Azeotropic Data III. Advances in Chemistry Series 116”, Ed. R.F. Gould, Am. Chem. Soc., Washington, (1973).
- Jang S.S., „Dynamic optimization of multicomponent batch distillation processes using continuous and discontinuous collocation polynomial policies”, Chem. Eng. J. 51 (2) 83–92. (1993).
- Jacobsen, E., L. Laroche, M. Morari, “Robust Control of Homogeneous Azeotropic Distillation Columns”, AIChE J., 37, 1810 (1991).
- Julka, V., & Doherty, M. F. „Geometric nonlinear analysis of multicomponent nonideal distillation: Asimple computer-aided design procedure”. Chemical Engineering Science, 48, 1367–1391. (1993).
- Kiva, V. N., & Serafimov, L. A. „Non-local rules of the movement of process lines for simple distillation in ternary systems [Rules that Govern the Residue Curve Trajectories for Ternary Mixtures]” Russian Journal of Physical Chemistry, 47(3), 638–642. (1973a).
- Kiva, V. N., & Serafimov, L. A.. „Batch distillation of ternary mixtures at constant reflux ratio, II. Analysis of the dynamic system of the distillate and the splitting into regions of distillation”, Russian Journal of Physical Chemistry, 47(3), 634–637. (1973b).
- Kiva, V. N., & Serafimov, L. A. „Localization of boundaries for batch distillation of ternary mixtures”,. Russian Journal of Physical Chemistry, 50(10), 2481–2483. (1976).
- Kogan, L. V., & Kafarov, V. V.. „Determination of the boundaries of rectification regions. Communication I”. Russian Journal of Applied Chemistry, 50(2), 302–305 [323–326]. (1977a).
- Kogan, L. V., & Kafarov, V. V. „Determination of the boundaries of rectification regions. Communication II.” Russian Journal of Applied Chemistry, 50(2), 306–309 [326–329]. (1977b).
- Kogan, V. B. „Azeotropic and extractive distillation (2nd ed.)”, Leningrad: Chemistry Publishing Co (in Russian). (1971).
- Komarova, L. F., Serafimov, L. A., & Garber, Yu. N. „Classification of ternary mixtures with biazeotropic constituents”, Russian Journal of Physical Chemistry, 48(6), 1391–1396 [817–818]. (1974).
- Kushner, T. M., Shulga, G. V., & Serafimov, L. A. „Evolution of VLE diagrams of biazeotropic binary mixtures with variation of pressure. In Paper collection: Problems of thermodynamics of heterogeneous systems and the theory of interfacial effects”, Issue 9, St. Petersburg University, St. Petersburg, pp. 64–81. (1992).
- Laroche, L., Bekiaris, N., Andersen, H.W., Morari, M., "Homogeneous azeotropic distillation:comparing entrainers", The Canadian Journal of Chemical Engineering, 69, 1302 (1991).
- Laroche, L., Bekiaris, N., Andersen, H.W., Morari, M., "The curious behavior of homogeneous azeotropic distillation – implications for entrainer selection", AIChE J., 38 (9) 1309 (1992).
- Laroche, L., Bekiaris, N., Andersen, H. W., & Morari, M. „Homogeneous Azeotropic distillation: Comparing entrainers”, Canadian Journal of Chemical Engineering, 69, 1302–1319. (1993).
- Levy, S. G., Van Dongen, D. B., & Doherty, M. F. „Design and synthesis of homogeneous azeotropic distillations. 2. Minimum reflux calculations for nonideal and azeotropic columns”, Industrial and Engineering Chemistry, Fundam, 24(4), 463–474. (1985).
- Lino M., Nakae A., Sudoh J., Hirata M., Hirose Y. „Removal of a small amount of methylene chloride in acetone by extractive distillation employing salt as separating agent”, Journal of Chemical Engineering of Japan, 4, 22, (1971).
- Kemény S., Thury É., Deák A., ”Állapotegyenletek fázisegyensúlyok számítására”, BME, (1991).
- Keyes D.B., ”The manufacture of anhydrous ethyl alcohol”, Ind. Eng. Chem., 21, 998-1001, (1929).
- Khanna N. K., Raczynski, R. F., Zudkevitch D. ”Distillation for separating dialkyl ketones from lower chlorohydrocarbons”, Allied Chemical Corp., USA, (1980).
- King, C.J., ”Separation Processes”, 2nd ed., Mc-Graw Hill, (1980).
- Kortüm G., A. Bittel, “Die Trennung primärer, sekundärer und tertiärer aromatischer Amine durch extractive Destillation I.-II.”, Chem. Ing. Technik, 28, 40, 282 (1956).
- Kovach J. W. and Seider, W. D., ”Heterogeneous Azeotropic Distillation: Experimental and Simulation Results” AICh J. 33, 1300, (1987a).
- Kovach J. W. and Seider, W. D., ”Heterogeneous Azeotropic Distillation:Homotopy-Continuation-Methods” Comp. Chem. Eng., 11, (1987b).
- Lang P., Yatim H., Moszkovicz P., Otterbein M., ”Batch extractive distillation under constant reflux ratio”, Comp. Chem. Eng., 18, 1057, (1994).
- Laroche L., Bekiaris N., Andersen H. W., Morari H., ”Homogeneous Azeotropic Distillation: Comparing Entrainers”, Can. J. Chem Eng. 69, 1302, (1991).
- Lecat M., ”Tables Azeotropic”, Monograph Lamertin, Brüsszel (1949).
- Lewis W. K. J., “The Efficiency and Design of Rectifying Column for Binary Mixtures”, Ind. Eng. Chem. Res., 14, 492 (1922).
- Malenko, Yu. I. „Physicochemical analysis of distillation diagrams. II. Quaternary mixtures”, Russian Journal of Physical Chemistry, 44(7), 916–918 [1631–1636]. (1970).
- Matsuyama H., H. J. Nishimura, "Topological and Thermodynamic Classification of Ternary Vapor-Liquid Equilibria", Chem. Eng. Jpn. 10, 181., (1977).
- Meadows E. L., “Multicomponent Batch Distillation Calculation on a Digital Computer”, Chem. Eng. Progr. Symp. Ser., 59, 48, (1963).
- Muller, E. „Liquid–liquid extraction”, (Vol. B3). Ullmann’s Enc. Ind. Chem. (1988).
- Napiorkowski W., Mazur W., Osmolski K., Kunicka T., Walewski K., ”Separation of mixtures of acetone and methylene chloride”, Tarchominskie Zaklady Farmaceutyczne "Polfa", Pol., (1981).
- Ostwald, W. „Lehrbuch der Allgemeinen Chemie”, Verwandtschaftslehre. Erste Teil. Leipzig, Germany: Verlag von Wilhelm Engelmann (in German). (1902).
- Othmer D. F. „Azotropic Distillation for dehydration acetic acid”, Chem. metall. Eng., 40, 91-95, (1941).
- Pham N. H. and M. F. Doherty, ”Design and Synthesis of Heterogeneous Azeotropic Distillations – I. Heterogeneous Phase Diagrams”, Chem. Eng. Sci., 45, 1823-1836, (1990a).
- Pham N. H. and M. F. Doherty, ”Design and Synthesis of Heterogeneous Azeotropic Distillations – II. Residue Curve Maps”, Chem. Eng. Sci., 45, 1837-1844, (1990b).
- Pham N. H. and M. F. Doherty, ”Design and Synthesis of Heterogeneous Azeotropic Distillations – III. Column Sequences”, Chem. Eng. Sci., 45, 1845-1854, (1990c).
- Pelkonen, S., Kaesemann, R., & GQorak, A.. „Distillation lines for multicomponent separation in packed columns: Theory and comparison with experiment”, Industrial and Engineering Chemistry Research, 36, 5392–5398. (1997).
- Petlyuk, F. B., Kievski, V. Ya., & Serafimov, L. A. „Thermodynamic and topologic analysis of the phase diagram of polyazeotropic mixtures. I. Definition of distillation regions using a computer [Computer-aided determination of azeotropic distillation regions]”, Russian Journal of Physical Chemistry, 69(12), 3102–3104. (1975a).
- Petlyuk, F. B., Kievski, V. Ya., & Serafimov, L. A. „Thermodynamic and topologic analysis of the phase diagram of polyazeotropic mixtures. I. Algorithm for construction of structural graphs for azeotropic ternary mixtures”. Russian Journal of Physical Chemistry, 69(12), 3105–3108. (1975b).
- Petlyuk, F. B., Kievski, V. Ya., & Serafimov, L. A. „Thermodynamic–topological analysis of VLE diagrams for multicomponent mixtures. III. Algorithm of structure graph drawing for four-component mixtures”, Russian Journal of Physical Chemistry, 71(2), 315–318. (1977a).
- Petlyuk, F. B., Kievskii, V. Ya., & Serafimov, L. A.. „A combined thermodynamic and topological analysis of phase equilibrium diagrams for polyazeotropic systems—V. The use of the phase equilibrium model in combined thermodynamic and topological analysis”, Russian Journal of Physical Chemistry, 51, 338–340. (1977b).
- Petlyuk, F. B., Kievski, V. Ya., & Serafimov, L. A. „Method for the isolation of the regions of recti6cation of polyazeotropic mixtures using an electronic computer [Computer-aided determination of distillation regions for multicomponent mixtures]”, Theoretical Foundations of Chemical Engineering, 11(1), 3–10. (1977c).
- Petlyuk, F. B., Kievski, V. Ya., & Serafimov, L. A. „Thermodynamic–topological analysis of VLE diagrams for multicomponent mixtures. IV. Use of the structure matrix for analysis of feasible separations of the wood pyrolysis product”, Russian Journal of Physical Chemistry, 72(5), 1145–1148. (1978).
- PPollmann, P., & Blass, E. „Best products of homogeneous azeotropic distillations”, Gas Separation and Purification, 8(4), 194–228. (1994).
- Prigogine, I., & Defay, R.. „Chemical thermodynamics”, London: Longmans & Green. (1954).
- Reinders, W., & de Minjer, C. H. „Vapour–liquid equilibria in ternary systems I. The course of the distillation lines”, Recueil des Travaux Chimiques, 59, 207–230. (1940).
- Reinders, W., & DeMinjer, C. H. „Vapour–liquid equilibria in ternary systems. II. The system acetone–chloroform–benzene”, Recueil des Travaux Chimiques, 59, 369–391. (1940a).
- Reinders, W., & DeMinjer, C. H. „Vapour–liquid equilibria in ternary systems. III. The course of the distillation lines in the system acetone–chloroform–benzene”, Recueil des Travaux Chimiques, 59, 392–406. (1940b).
- Reinders, W., & DeMinjer, C. H.. „Vapour–liquid equilibria in ternary systems. IV. The system water–acetone–thrichloroethene”. Recueil des Travaux Chimiques, 66(9/10), 552–563. (1947a).
- Reinders, W., & DeMinjer, C. H. „Vapour–liquid equilibria in ternary systems. V. The system water–formic acid–metaxylene”, Recueil des Travaux Chimiques, 66(9/10), 564–572. (1947b).
- Reinders, W., & DeMinjer, C. H. „Vapour–liquid equilibria in ternary systems. VI. The system water–acetone–chloroform”, Recueil des Travaux Chimiques, 66(9/10), 573–604. (1947c).
- Reshetov, S. A., Sluchenkov, V. Yu., Ryzhova, V. S., & Zhvanetskij, I. B. „Diagrams of K-ordering regions with an arbitrary number of unitary !-lines [Univolatility lines]”. Russian Journal of Physical Chemistry, 64(9), 1344–1347 [2498–2503]. (1990).
- Robbins L. A., Chem. Eng. Prog., 76 (10) 58-61, (1980).
- Sadomoto, H., and K. Miyahara, “Calculation Procedure for Multicomponent Batch Distillation,” Int. Chem. Eng., 23, 56 (1983).
- Schreinemakers F. A. H. “Dampfdrucke Ternarer Gemische. Theoretischer Teil: Dritte Abhandlung”, Z. Phys. Chem., 36, 710-740, (1901a).
- Schreinemakers F. A. H. “Dampfdrucke Ternarer Gemische. Theoretischer Teil: Erste Abhandlung”, Z. Phys. Chem., Stoechiom. Verwandtschaftsl, 36, 2257-289, (1901b).
- Schreinemakers F. A. H., “Dampfdrucke Ternarer Gemische. Theoretischer Teil: Zweite Abhandlung”, Z. Phys. Chem., Stoechiom. Verwandtschaftsl, 36, 413-449, (1901c).
- Schreinemakers F. A. H., “Einige Bemerkungen uber Dampfdrucke”, Z. Phys. Chem., Stoechiom. Verwandtschaftsl, 43, 671-685, (1902).
- Serafimov, L. A. „The azeotropic rule and the classification of multicomponent mixtures. III. Distribution of singular points in the phase diagram for liquid–vapor equilibrium in four-component mixtures”, Russian Journal of Physical Chemistry, 42(1), 132–135 [252–256]. (1968c).
- Serafimov, L. A. „Separation technology of azeotropic mixtures”. In W. QSwiYetos lawski (Ed.), Azeotropy and polyazeotropy, Chapter XX1 (additional chapter in Russian edition). Moscow: Chemistry Publishing Co., pp. 186–224. (1968a).
- Serafimov, L. A. „The azeotropic rule and the classi6cation of multicomponent mixtures. II. The form [pattern] of distillation lines [residue curves] near four-component singular points”. Russian Journal of Physical Chemistry, 42(1), 130–131 [248–252]. (1968b).
- Serafimov, L. A. „Theoretical principles of distillation sequences design and synthesis for nonideal multicomponent mixtures”. Ph.D. thesis, Lomonosov Institute of Fine Chemical Technology, Moscow (in Russian). (1968d).
- Serafimov, L. A. „The azeotropic rule and the classification of multicomponent mixtures. IV. Pricipal equations for the calculation of liquid–vapor phase equilibrium diagrams for four-component mixtures”, Russian Journal of Physical Chemistry, 43(3), 621–624. (1969a).
- Serafimov, L. A. „The azeotropic rule and the classification of multicomponent mixtures V. Analysis of liquid–vapor phase equilibrium diagrams for quaternary mixtures”, Russian Journal of Physical Chemistry, 43(5), 749–751 [1343–1346]. (1969b).
- Serafimov, L. A. „The azeotropic rule and the classi6cation of multicomponent mixtures VI. n-Component mixtures”, Russian Journal of Physical Chemistry, 43(7), 981–983. (1969c).
- Serafimov, L. A. „General principles of the course of unidistribution lines in vapor–liquid equilibrium diagrams of ternary mixtures”, Physical–chemical foundations of rectification, collection of papers by Moscow Lomonosov Institute of Fine Chemical Technology, MITChT, Moscow, pp. 20–30. (1970a).
- Serafimov, L. A. „The azeotropic rule and the classification of multicomponent mixtures VII. Diagrams for ternary mixtures”, Russian Journal of Physical Chemistry, 44(4), 567–571 [1021–1027]. (1970b).
- Serafimov, L. A. „The azeotropic rule and the classification of multicomponent mixtures. VIII. The general relations of tangential azeotropy”. Russian Journal of Physical Chemistry, 45(5), 638–642 [1140–1147]. (1971a).
- Serafimov, L. A.. „The azeotropic rule and the classi6cation of multicomponent mixtures. IX. Tangential azeotropy and correlation between the general relation between singular points of various types”, Russian Journal of Physical Chemistry, 45(6), 831–833 [1473–1476]. (1971b).
- Serafimov, L. A. „The azeotropic rule and the classi6cation of multicomponent mixtures. X. Doubly tangential azeotropes”, Russian Journal of Physical Chemistry, 45(6), 918–921 [1620–1625]. (1971c).
- Serafimov, L. A. „The azeotropic rule and the classi6cation of multicomponent mixtures. XI. Tangential azeotropy for three-component systems and chains of topological structures”, Russian Journal of Physical Chemistry, 45(10), 1388–1389 [2448–2450]. (1971d).
- Serafimov, L. A., Gol’berg, Yu. E., Vitman, T. A., & Kiva, V. N. „Properties of univolatility sets and its location in the concentration space In Chemistry”, Collection of the Scientific Works of Ivanovo Energetic Institute, Ivanovo-Vladimir, Issue 14, pp. 166–179 (in Russian). (1972).
- Serafimov, L. A., Komarova, L. F., & Garber, Yu. N. „Classification of VLE diagrams for ternary mixtures with biazeotropic constituents”, Russian Journal of Physical Chemistry, 48(6), 1391. (1974).
- Serafimov, L. A., Timofeyev, V. S., & Balashov, M. I. „Rectification of multicomponent mixtures II. Local and general characteristics of the trajectories of rectification processes at infinite reflux ratio”. Acta Chemica Academiac Scientarium Hungaricae, 75(2), 193–211. (1973).
- Serafimov, L. A., Zharov, V. T., & Timofeyev, V. S. „Rectification of multicomponent mixtures I. Topological analysis of liquid–vapor phase equilibrium diagrams”. Acta Chemica Academiac Scientarium Hungaricae, 69(4), 383–396. (1971).
- Tanaka, S. and J. Yamada, “Graphical calculation method for minimum reflux ratio in azeotropic distillation,” J. Chem. Eng. Japan, 5, 20 (1972).
- Treybal R. E. ”Mass-Transfer Operations”, 2nd edition, McGraw-Hill, New York, 395, (1968).
- Van Dongen D. B., and M. F. Doherty, ”Design and Synthesis of Homogeneous Azeotropic Distillations. 1 Problem Formulation for a Single Distillation Column”, Ind. Eng Chem.. Res., 24, 454, (1985).
- Van Dongen D.B., M.F. Doherty, „On the dynamics of distillation process. VI. Batch distillation”, Chem. Eng. Sci. 40 2087–2093. (1985).
- Wahnschafft O.M., J.W. Koehler, E. Blass and A.W Westerberg, ”The product Composition Rewgions of Single-Feed Azeotropic Distillation Columns”, Ind. Eng. Chem. Res., 31, 2345. (1992).
- Wahnschaff, 0. M., and A. W. Westerberg, “The Product Composition Regions of Azeotropic Distillation Columns. 2. Separability in Two-Feed Columns and Entrainer Selection,” Ind. Eng. Chem. Res., 32, 1108 (1993).
- Warter, M., Stichlmair, J., Batchwise extractive distillation in a column with a middle vessel, Comp. Chem. Eng., 23, S915 (1999).
- Wentworth T. O., D.F Othmer, ”Absolute alcohol, an economical method for its manufacture”, Trans. Am. Inst. Chem. Engn. 36, 785-799, (1940).
- Widagdo S., W.D. Seider, D.H. Debastian, ”Dynamic analysis of heterogeneous azeotropic distillation”, AIChE J., 38, 1229, (1992).
- Woodman M. R., W. Morton, W. R. Paterson, ”Simulation of the Distillation of Three Phase Mixtures”, CHISA 90, (1990).
- Yatim H., P. Moszkowicz, M. Otterbein and P. Lang, ”Dynamic simulation of a batch extractive distillation process”, Comp. Chem. Eng., 17, S57, (1993).
- Young S., ”The preparation of absolute alcohol from strong spirit”, J. Chem. Soc., 81, 707-717, (1902).
- Zharov V.T and L.A. Serafimov, ”Physicochemical Foundations of Simple Distillation and Rectification”, Chemistry Publishing Co., (1975).
- Zharov, V. T., "Free evaporation of homogeneous multicomponent solutions", Russ. J. Phys. Chem., 41, 1539 (1967)
Kezdőlap Definíciók Cikkek Könyvek Linkek Konferenciák Kapcsolat - Design by GM 2006 -