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Partial oxidation of ethane: the potential of membrane reactors. Journal of the University of Chemical Technology and Metallurgy 202.
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82, S. 25 - 40 (2003)
Concentration and residence time effects in packed bed membrane reactors. Catalysis today 203.
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42 (26), S. 6949 - 6955 (2003)
Nonlinear oscillations in ammonium sulphate crystallization: a comparison of different model predictions. Industrial and Engineering Chemistry Research 204.
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1006, S. 3 - 13 (2003)
Optimal operation of simulated moving bed chromatographic processes by means of simple feedback control. Journal of Chromatography A 205.
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1006, S. 77 - 86 (2003)
Simulated moving bed process with cyclic modulation of the feed concentration. Journal of Chromatography A 206.
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75 (4), S. 379 - 383 (2003)
Verbesserter Betrieb von Simulated Moving Bed-Prozessen durch zyklische Modulation der Feedkonzentration. Chemie-Ingenieur-Technik 207.
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58, S. 5217 - 5227 (2003)
Improved operation of simulated moving bed processes through cyclic modulation of feed flow and feed concentration. Chemical Engineering Science 208.
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58, S. 2203 - 2214 (2003)
Multiple steady states in two-phase reactors under boiling conditions. Chemical Engineering Science 209.
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42, S. 3294 - 3303 (2003)
Nonlinear behavior of reactor-separator networks: influence of separator control structure. Industrial & Engineering Chemistry Research 210.
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57 (19), S. 4099 - 4116 (2002)
A network theory for the structured modelling of chemical processes. Chemical Engineering Science 211.
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57 (20), S. 4391 - 4399 (2002)
A numerical bifurcation analysis of nonlinear oscillations in crystallization processes. Chemical Engineering Science 212.
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26 (2-3), S. 147 - 163 (2002)
Reactive separation of isobutene from C4 crack fractions by catalytic distillation processes. Separation and Purification Technology 213.
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25 (12), S. 1151 - 1155 (2002)
Improving simulated moving bed processes by cyclic modulation of the feed concentration. Chemical Engineering and Technology 214.
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216 (4), S. 403 - 433 (2002)
Yield effects in single and coupled nonlinear thermokinetic reaction systems. Zeitschrift für Physikalische Chemie 215.
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4 (24), S. 5988 - 5994 (2002)
Stochastic resonance in a thermokinetic reaction system. Physical Chemistry Chemical Physics 216.
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56 (18), S. 5239 - 5254 (2001)
A theoretical study of kinetic instabilities in catalytic distillation: Influence of transport limitations inside the catalyst. Chemical Engineering Science 217.
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56 (8), S. 2837 - 2849 (2001)
Nonlinear behaviour of an ideal reactor separator network with mass recycle. Chemical Engineering Science 218.
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105 (30), S. 7216 - 7224 (2001)
Experimentally Coupled Thermokinetic Oscillators: Phase Death and Rhythmogenesis. Journal of Physical Chemistry A 219.
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55, S. 1817 - 1828 (2000)
Low-order dynamic models for ideal multicomponent distillation processes using nonlinear wave propagation theory. Chemical Engineering Science 220.
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28 (3-4), S. 209 - 221 (2000)
Catalysts from waste materials. Applied Catalysis B: Environmental 221.
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55 (2), S. 441 - 454 (2000)
Nonlinear computation using DIVA - methods and applications. Chemical Engineering Science 222.
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107 (13), S. 68 - 72 (2000)
Separation using coupled reactive distillation columns. Chemical Engineering 223.
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2 (16), S. 3605 - 3612 (2000)
The Behavior of the Iron(III)-Catalyzed Oxidation of Ethanol by Hydrogen Peroxide in a Fed-Batch reactor. Physical Chemistry Chemical Physics 224.
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47 (10), S. 501 - 508 (1999)
Sensitivitätsbasierte Erkennung gefährlicher Zustände in Reaktoren. at - Automatisierungstechnik 225.
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Optimization of a reactor network for ethylene glycol synthesis: an algorithmic approach. Computers and Chemical Engineering 226.
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Object-oriented modeling of distillation processes. Computers and Chemical Engineering 227.
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The Iron (III)-catalyzed oxidation of ethanol by hydrogen peroxide: a thermokinetic oscillator. Journal of Physical Chemistry 228.
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Simulation and nonlinear analysis of a LDPE Tubular reactor (in Russian). In: Problems of Simulation and Computer Aided Design of Dynamical Systems (SCAD-2012), S. 1 - 10 (Hg. Donetsk National Technical University). Donetsk National Technical University, Donetsk (2012)
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Model Reduction and State Estimation. In: Molten Carbonate Fuel Cells: Modeling, Analysis, Simulation, and Control, S. 185 - 200 (Hg. 245.
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Hot Spot Formation and Steady State Multiplicities. In: Molten Carbonate Fuel Cells: Modeling, Analysis, Simulation, and Control, S. 141 - 163 (Hg. 246.
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Nonlinear Model Reduction of a Dynamic Two-dimensional Molten Carbonate Fuel Cell Model. In: Progress in Industrial Mathematics at ECMI 2004, S. 262 - 266 (Hg. Di Bucchianico, A.; Mattheij, R. M. M.; Peletier, M. A.). Springer, Berlin [u.a.] (2006)
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Equilibrium Theory and Nonlinear Waves for Reaction Separation Processes. In: Integrated Chemical Processes, S. 149 - 181 (Hg.
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Real-time optimization for large scale processes: Nonlinear model predictive control of a high purity distillation column. In: Online Optimization of Large Scale Systems, S. 363 - 383 (Hg. Grötschel, M.; Krumke, S. O.; Rambeau, J.). Springer-Verlag (2001)