Publikationsliste Prof. Dr.-Ing. Achim Kienle - Max-Planck-Institut für ...
Publikationsliste Prof. Dr.-Ing. Achim Kienle - Max-Planck-Institut für ...
Publikationsliste Prof. Dr.-Ing. Achim Kienle - Max-Planck-Institut für ...
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[124] Mohl, K. D., <strong>Kienle</strong>, A., Gilles, E. D., Rapmund, P., Sundmacher, K., und Hoffmann, U.: Multiple<br />
steady states for the production of fuel ethers MTBE and TAME via reactive distillation – Theoretical<br />
and experimental results. Proc. AIChE Ann. Meeting, Paper 220c, November 15-20, Miami Beach<br />
1998.<br />
[125] Sundmacher, K., Hoffmann, U., Rapmund, P., Mohl, K. D., <strong>Kienle</strong>, A., und Gilles, E. D.: Nachweis<br />
mehrfacher stationärer Betriebszustände einer gepackten Reaktivdestillationskolonne <strong>für</strong> die Herstellung<br />
der Kraftstoffkomponente tert-Amylmethylether (TAME). Chem.-<strong>Ing</strong>.-Tech. 70 (1998), S.<br />
1099.<br />
[126] <strong>Kienle</strong>, A., Mangold, M., Mohl, K. D., und Gilles, E. D.: Nonlinear computation using DIVA – Methods<br />
and applications. Proc. CHISA’98, Paper 312, 23.-28. August, Praha, Czech Republic, 1998.<br />
[127] Stein, E., <strong>Kienle</strong>, A., Esparta, R., Mohl, K. D., und Gilles, E. D.: Optimization of a reactor network<br />
for ethylene glycol synthesis. Proc. CHISA’98, Paper 108, 23.-28. August, Praha, Czech Republic,<br />
1998.<br />
[128] <strong>Kienle</strong>, A.: Reduced models for multicomponent separation processes using nonlinear wave propagation<br />
theory. Proc. CHISA’98, Paper 109, 23.-28. August, Praha, Czech Republic, 1998.<br />
[129] Klein, E., <strong>Kienle</strong>, A., und Raisch, J.: Synthesizing a supervisory control system for the start-up procedure<br />
of a distillation column – an approach based on approximating continuous dynamics by DES<br />
models. Proc. LSS’98 Symposium on Large Scale Systems: Theory and Application, IFAC. 1998, S.<br />
716–721.<br />
[130] Stein, E., <strong>Kienle</strong>, A., und Gilles, E. D.: Dynamic optimization of multicomponent distillation processes.<br />
In: Scientific Computing in Chemical Engineering II (Hrsg.: Keil, F., Mackens, W., Voß, H., und<br />
Werther, J.), Springer-Verlag, Berlin, Heidelberg, New York 1999, S. 362–369.<br />
[131] <strong>Kienle</strong>, A., Stein, E., Rehm, A., und Kloppenburg, E.: Low-order dynamic models for two coupled<br />
distillation columns. Proc. European Control Conference ECC’99, Paper F1004-4, 31. August - 3.<br />
September, Karslruhe 1999.<br />
[132] Waschler, R., <strong>Kienle</strong>, A., Svjatnyj, V., Gilles, E. D., Anoprienko, A., und Osipova, T.: Modeling and<br />
simulation of a chemical reactor for the production of acetic acid. III dynamic phase transitions. Proc.<br />
Problems of simulation and computer aided design of Dynamic Systems, 1999, S. 102–109.<br />
[133] Klein, E., Wehlan, H., Raisch, J., und <strong>Kienle</strong>, A.: Synthese einer Anfahrregelung <strong>für</strong> eine Destillationskolonne<br />
auf der Grundlage einer ereignisdiskreten Approximation der kontinuierlichen Dynamik.<br />
Proc. EKA’99 - 6. Fachtagung Entwicklung und Betrieb komplexer Automatisierungssysteme, Mai<br />
27-28, Braunschweig 1999, S. 447–464.<br />
[134] Klein, E., Itigin, A., Raisch, J., und <strong>Kienle</strong>, A.: Automatic generation of switching startup schemes<br />
for chemical processes. Proc. European Symposium on Computer Aided Process Engineering – 10<br />
(Hrsg.: Pierucci, S.), Elsevier. 2000, S. 619–624.<br />
[135] <strong>Kienle</strong>, A.: Nonlinear model reduction for nonreactive and reactive distillation processes using nonlinear<br />
wave propagation theory. Proc. SPC-2000, Third Symposium on Process Control, Ploiesti,<br />
Romania 2000, S. 72–78.<br />
[136] Stein, E., <strong>Kienle</strong>, A., Kolah, A., Qi, Z., Sundmacher, K., und Mohl, K. D.: Production of high purity isobutene<br />
using coupled reactive distillation columns. Proc. AIChE Ann. Meeting, Paper 245f, November<br />
12-17, Los Angeles 2000.<br />
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