12.07.2015 Views

Modelling reactive distillation

Modelling reactive distillation

Modelling reactive distillation

SHOW MORE
SHOW LESS

Create successful ePaper yourself

Turn your PDF publications into a flip-book with our unique Google optimized e-Paper software.

5222 R. Taylor, R. Krishna / Chemical Engineering Science 55 (2000) 5183}5229Altiqi, I., Sabri, M. F., Bouhamra, W., & Alper, E. (1994). Steady-staterate-based modelling for CO /amine absorption-desorption systems.Gas Separation and Purixcation, 8, 3}11.Asselineau, L., Mikitenko, P., Viltard, J. C., & Zuliani, M. (1994) U.S.Patent 5368691: Reactive <strong>distillation</strong> process and apparatus forcarrying it outBabcock, P. D., & Clump, C. W. (1978). Distillation of chemically<strong>reactive</strong> solutions. In N.N. Li, Recent developments in separationscience, vol. IV (pp. 149}166).Backhaus, A. A. (1921). Continuous processes for the manufacture ofesters, US patent 1400849.Backhaus, A. A. (1922). Apparatus for producing high grade esters, USpatent 1403224.Backhaus, A. A. (1923a). Process for producing high grade esters, USpatent 1454462.Backhaus, A. A. (1923b). Process for esteri"cation, US patent 1454463.Balashov, M. I., Patlasov, V. P., & Sera"mov, L. A. (1981). Rules ofprimary reaction zone spread in continuous combined reactionfractionationprocess. Theoretical Foundations of Chemical Engineering,15, 406}413.Balashov, M. I., & Sera"mov, L. A. (1980). The statics analysis ofcontinuous combined reaction-fractionation process. TheoreticalFoundations of Chemical Engineering, 14, 803}808.Barbosa, D., & Doherty, M. F. (1987a). Theory of phase diagrams andazeotropic conditions for two-phase <strong>reactive</strong> systems. Proceedingsof the Royal Society London A, 413, 443}458.Barbosa, D., & Doherty, M. F. (1987b). A new set of compositionvariables for the representation of <strong>reactive</strong> phase diagrams. Proceedingsof the Royal Society London A, 413, 459}464.Barbosa, D., & Doherty, M. F. (1988a). The in#uence of equilibriumchemical reactions on vapor liquid-phase diagrams. Chemical EngineeringScience, 43, 529}540.Barbosa, D., & Doherty, M. F. (1988b). The simple <strong>distillation</strong> ofhomogeneous <strong>reactive</strong> mixtures. Chemical Engineering Science, 43,541}550.Barbosa, D., & Doherty, M. F. (1988c). Design and minimum re#uxcalculations for single-feed multicomponent <strong>reactive</strong> <strong>distillation</strong> columns.Chemical Engineering Science, 43, 1523}1537.Barbosa, D., & Doherty, M. F. (1988d). Design and minimum re#uxcalculations for double-feed multicomponent <strong>reactive</strong> <strong>distillation</strong>columns. Chemical Engineering Science, 43, 2377}2389.Barbosa, D., & Doherty, M. F. (1990). Theory of phase diagrams andazeotropic conditions for two-phase <strong>reactive</strong> systems. Proceedingsof the Royal Society London A, 430, 669}678.Bart, H. -J., & LandschuK tzer, H. (1996). Heterogene Reaktivdestillationmit axialer RuK ckvermischung. Chemie Ingenieur Technik, 68,944}946.Bart, H. -J., & Reidetschlager, J. (1995). Distillation with chemicalreactionand apparatus selection. Separaration Science and Technology,30, 1849}1865.Bart, H. -J., & Resil, H. -O. (1997). Der Hybridprozess Reaktivdestillation/Pervaporationzur Herstellung von CarbonsaK ureestern.Chemie Ingenieur Technik, 69, 824}827.Bartlett, D. A., & Wahnscha!t, O. M. (1998). Dynamic simulation andcontrol strategy evaluation for MTBE <strong>reactive</strong> <strong>distillation</strong>. In J.F.Pekny & G.E. Blau, Foundations of computer-aided process operation,AIChE Symposium Series, vol. 320, (pp. 315}321).Van Baten, J. M., & Krishna, R. (2000). <strong>Modelling</strong> of sieve tray hydraulicsusing computational #uid dynamics. Chemical Engineering Journal,77, 143}152.Baur, R., Higler, A. P., Taylor, R., & Krishna, R. (1999). Comparison ofequilibrium stage and nonequilibrium stage models for <strong>reactive</strong><strong>distillation</strong>. Chemical Engineering Journal, 76, 33}47.Belck, L. H. (1955). Continuous reactions in <strong>distillation</strong> equipment.American Institute of Chemical Engineers Journal, 1, 467}470.Berman, S., Isbenjian, H., Sedo!, A., & Othmer, D. F. (1948a). Esteri"-cation. Continuous production of Dibutyl phthalate in a <strong>distillation</strong>column. Industrial and Engineering Chemistry, 40, 2139}2148.Berman, S., Melnychuk, A., & Othmer, D. F. (1948b). Dibutylphthalate. Reaction rate of catalytic esteri"cation. Industrial andEngineering Chemistry, 40, 1312}1319.Bessling, B., Loning, J. -M., Ohligschlager, A., Schembecker, G., & Sundmacher,K. (1998). Investigations on the synthesis of methyl acetatein a heterogeneous <strong>reactive</strong> <strong>distillation</strong> process. Chemical Engineeringand Technolgy, 21, 393}400.Bessling, B., Schembecker, G., & Simmrock, K. H. (1997a). Design ofprocesses with <strong>reactive</strong> <strong>distillation</strong> line diagrams. Industrial andEngineering Chemistry Research, 36, 3032}3042.Bessling, B., Schembecker, G., & Simmrock, K. H. (1997b). Design of<strong>reactive</strong> <strong>distillation</strong> processes with <strong>reactive</strong> and non<strong>reactive</strong> <strong>distillation</strong>zones. Distillation and absorption '97, Institute of ChemicalEngineers Symposium Series, vol. 142 (pp. 675}684).Bezzo, F., Bertucco, A., Forlin, A., & Barolo, M. (1999). Steady-stateanalysis of an industrial <strong>reactive</strong> <strong>distillation</strong> column. Separation andPurixcation Technology, 16, 251}260.Block, U. (1977). Carrying out continuous reactions with superposed<strong>distillation</strong>. Chemie Ingenieur Technik, 49(2), 151.Block, U., & Hegner, B. (1977). Simulationsmethode fur homogeneFlussigphasenreacktion mit uberlagerter Destillation. Verfahrenstechnik,11(2), 101}104.Bock, H., & Wozny, G. (1997). Analysis of <strong>distillation</strong> and reactionrate in <strong>reactive</strong> <strong>distillation</strong>. Distillation and absorption '97. Instituteof Chemical Engineers Symposium Series, vol. 142 (pp.553}564).Bogacki, M. B., Alejski, K., & Szymanowski, J. (1989). The fast methodof the solution of a reacting <strong>distillation</strong> problem. Computers andChemical Engineering, 13, 1081}1085.Bollyn, M. P., & Wright, A. R. (1998). Development of a <strong>reactive</strong>process model for a batch <strong>reactive</strong> <strong>distillation</strong> * a case study.Computers and Chemical Engineering, 22, S87}S94.Bondy, R. W. (1991) Physical continuation approaches to solving<strong>reactive</strong> <strong>distillation</strong> problems. Paper presented at the AIChE meeting,Los Angeles.Bravo, J. L., Pyhalathi, A., & Jaervelin, H. (1993). Investigations ina catalytic <strong>distillation</strong> pilot plant: Vapor/ liquid equilibrium, kineticsand mass transfer issues. Industrial and Engineering ChemistryResearch, 32, 2220}2225.Buchholz, M., Pinaire, R., & Ulowetz, M. A. (1995). Structure andmethod for catalytically reacting #uid streams in mass transferapparatus, European patent 448884B1.Buzad, G., & Doherty, M. F. (1994). Design of three componentkinetically controlled <strong>reactive</strong> <strong>distillation</strong> systems using "xed-pointmethods. Chemical Engineering Science, 49, 1947}1963.Buzad, G., & Doherty, M. F. (1995). New tools for the design ofkinetically controlled <strong>reactive</strong> <strong>distillation</strong> columns for ternary mixtures.Computers and Chemical Engineering, 19, 395}408.Carey, T. T., Hermes, J. E., & Rochelle, G. T. (1991). A model of acid gasabsorption/stripping using MDEA with added acid. Gas Separationand Purixcation, 5, 95}109.Carland, R. J. (1994). Fractionation tray for catalytic <strong>distillation</strong>, USpatent 5308451.Carra, S., Morbidelli, M., Santacesaria, E., & Buzzi, G. (1979a). Synthesisof propylene oxide from propylene chlorohydrins * II.Modeling of the <strong>distillation</strong> with chemical reaction unit. ChemicalEngineering Science, 34, 1133}1140.Carra, S., Santacesaria, E., Morbidelli, M., & Cavalli, L. (1979b).Synthesis of propylene oxide from propylene-chlorohydrins* I Kinetic aspects of the process. Chemical Engineering Science, 34,1123}1132.Chang, Y. A., & Seader, J. D. (1988). Simulation of continuous <strong>reactive</strong><strong>distillation</strong> by a homotopy continuation method. Computers andChemical Engineering, 12, 1243}1255.Ciric, A. R., & Gu, D. (1994). Synthesis of nonequilibrium <strong>reactive</strong><strong>distillation</strong> by MINLP optimization. American Institute of ChemicalEngineers Journal, 40, 1479}1487.

Hooray! Your file is uploaded and ready to be published.

Saved successfully!

Ooh no, something went wrong!