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Two-Dimensional Model for Oxidative Coupling of Methane in a Packed-Bed Membrane Reactor.
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- Chemical Engineering & Technology, 2012, v. 35, n. 2, p. 294, doi. 10.1002/ceat.201100473
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Computational Approach to Characterize the Mass Transfer between the Counter-Current Gas-Liquid Flow.
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- Chemical Engineering & Technology, 2009, v. 32, n. 8, p. 1227, doi. 10.1002/ceat.200900099
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Portraying the Countercurrent Flow on Packings by Three-Dimensional Computational Fluid Dynamics Simulations.
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- Chemical Engineering & Technology, 2008, v. 31, n. 10, p. 1445, doi. 10.1002/ceat.200800273
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Legionella Control in Cooling Towers by Electrolytic Disinfection.
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- Chemical Engineering & Technology, 2005, v. 28, n. 7, p. 761
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Reduction of the Water Demand in the Process Industry by Production-Integrated Application of the Catalytic ElectrolysisLecture presented at the 5th GVC-Abwasser-Kongress “Prozessintegrierte und additive Verfahren der Abwasser- und Schlammbehandlung”, Sep. 22–24, 2003, Bremen (Germany).
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- Chemical Engineering & Technology, 2004, v. 27, n. 7, p. 747
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Optimal Production Planning for Chemical Processes under Uncertain Market Conditions.
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- Chemical Engineering & Technology, 2004, v. 27, n. 6, p. 641
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Influence of the Column Design on the HPLC (High Performance Liquid Chromatography) Process.
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- Chemical Engineering & Technology, 2004, v. 27, n. 4, p. 369
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CFD Simulation of Preparative HPLC Columns with Consideration of Nonlinear Isotherms.
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- Chemical Engineering & Technology, 2003, v. 26, n. 6, p. 651
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Analysis of the Start-up Process for Reactive Distillation.
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- Chemical Engineering & Technology, 2003, v. 26, n. 1, p. 81, doi. 10.1002/ceat.200390012
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Experimental Investigations of Three-Phase Distillation in a Packed Column.
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- Chemical Engineering & Technology, 2002, v. 25, n. 5, p. 513, doi. 10.1002/1521-4125(200205)25:5<513::AID-CEAT513>3.0.CO;2-8
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Heterogeneous Azeotropic Distillation in Packed Columns: Experimental Results.
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- Chemical Engineering & Technology, 2000, v. 23, n. 12, p. 1047, doi. 10.1002/1521-4125(200012)23:12<1047::AID-CEAT1047>3.0.CO;2-H
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Development and Experimental Verification of a Time-optimal Startup Strategy for a High Purity Distillation Column.
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- Chemical Engineering & Technology, 2000, v. 23, n. 10, p. 841, doi. 10.1002/1521-4125(200010)23:10<841::AID-CEAT841>3.0.CO;2-E
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Robuste Führung von nichtstationären Reaktionsprozessen unter Berücksichtigung von Unsicherheiten.
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- Chemie Ingenieur Technik (CIT), 2004, v. 76, n. 9, p. 1366, doi. 10.1002/cite.200490265
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- Article
Modellgestützte Messdatenverarbeitung zur Echtzeitoptimierung eines industriellen Koksofengasreinigungsprozesses.
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- Chemie Ingenieur Technik (CIT), 2004, v. 76, n. 9, p. 1358, doi. 10.1002/cite.200490258
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Aufreißende Filmströmung auf geneigten Oberflächen.
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- Chemie Ingenieur Technik (CIT), 2004, v. 76, n. 8, p. 1065, doi. 10.1002/cite.200403416
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Produktionsintegrierter Einsatz der katalytischen Elektrolyse zur Reduzierung des Wasserbedarfs in der Prozessindustrie.
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- Chemie Ingenieur Technik (CIT), 2004, v. 76, n. 6, p. 826, doi. 10.1002/cite.200403348
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Optimierung der Prozessführung in Chemieanlagen aus Sicht der Universität.
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- Chemie Ingenieur Technik (CIT), 2003, v. 75, n. 8, p. 990, doi. 10.1002/cite.200390171
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Nichtlineare stochastische Optimierung unter Unsicherheiten.
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- Chemie Ingenieur Technik (CIT), 2003, v. 75, n. 7, p. 814, doi. 10.1002/cite.200306137
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Optimale Produktionsplanung für verfahrenstechnische Prozesse unter unsicheren Marktbedingungen.
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- Chemie Ingenieur Technik (CIT), 2003, v. 75, n. 7, p. 832, doi. 10.1002/cite.200300048
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Einflüsse der Säulenkonstruktion auf den HPLC-Prozess.
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- Chemie Ingenieur Technik (CIT), 2003, v. 75, n. 4, p. 359, doi. 10.1002/cite.200390072
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Anfahren dreiphasiger Rektifikationskolonnen: Simulation und Experiment.
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- Chemie Ingenieur Technik (CIT), 2003, v. 75, n. 3, p. 194, doi. 10.1002/cite.200390038
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Wege zum Informationsmanagement für interdisziplinäre Forschungsprojekte und die Entwicklung eines prototypischen Systems.
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- Chemie Ingenieur Technik (CIT), 2002, v. 74, n. 11, p. 1545, doi. 10.1002/1522-2640(20021115)74:11<1545::AID-CITE1545>3.0.CO;2-X
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Analyse des Anfahrprozesses bei der Reaktivrektifikation.
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- Chemie Ingenieur Technik (CIT), 2002, v. 74, n. 9, p. 1253, doi. 10.1002/1522-2640(20020915)74:9<1253::AID-CITE1253>3.0.CO;2-B
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Anfahren von Reaktivrektifikationskolonnen.
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- Chemie Ingenieur Technik (CIT), 2002, v. 74, n. 5, p. 604, doi. 10.1002/1522-2640(200205)74:5<604::AID-CITE604>3.0.CO;2-F
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Deterministische und wissensbasierte Modelle für druckgetriebene Membranverfahren zur Einbindung in CAE-Werkzeuge.
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- Chemie Ingenieur Technik (CIT), 2002, v. 74, n. 5, p. 641, doi. 10.1002/1522-2640(200205)74:5<641::AID-CITE1111641>3.0.CO;2-3
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Wertstoffrückgewinnung und Reduzierung der Abwasserentsorgungskosten in einem Werk der Waschmittelproduktion.
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- Chemie Ingenieur Technik (CIT), 2002, v. 74, n. 4, p. 442, doi. 10.1002/1522-2640(200204)74:4<442::AID-CITE442>3.0.CO;2-J
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CFD-Simulation von präparativen Chromatographiesäulen unter Berücksichtigung von Adsorptionsisothermen.
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- Chemie Ingenieur Technik (CIT), 2002, v. 74, n. 3, p. 294, doi. 10.1002/1522-2640(200203)74:3<294::AID-CITE294>3.0.CO;2-3
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Design and Optimization of the Technical Chromatographic Process.
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- Chemie Ingenieur Technik (CIT), 2001, v. 73, n. 6, p. 721, doi. 10.1002/1522-2640(200106)73:6<721::AID-CITE7211111>3.0.CO;2-7
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Integral Optimization of an Industrial Batch Process.
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- Chemie Ingenieur Technik (CIT), 2001, v. 73, n. 6, p. 631, doi. 10.1002/1522-2640(200106)73:6<631::AID-CITE6313333>3.0.CO;2-S
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Vergleichende Betrachtung der Dreiphasenrektifikation in Boden- und Packungskolonnen.
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- Chemie Ingenieur Technik (CIT), 2000, v. 72, n. 9, p. 961, doi. 10.1002/1522-2640(200009)72:9<961::AID-CITE9610>3.0.CO;2-P
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Optimierung des Strömungsprofils in technischen Chromatographie-Säulen.
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- Chemie Ingenieur Technik (CIT), 2000, v. 72, n. 9, p. 967, doi. 10.1002/1522-2640(200009)72:9<967::AID-CITE9672>3.0.CO;2-W
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Untersuchung der Prozessdynamik komplexer thermischer Trennprozesse am Beispiel der chemischen Absorption/Desorption.
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- Chemie Ingenieur Technik (CIT), 2000, v. 72, n. 9, p. 1010, doi. 10.1002/1522-2640(200009)72:9<1010::AID-CITE10102>3.0.CO;2-4
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Abwassermanagement bei Cleaning-in-Place-Prozessen unter Berücksichtigung von Produktrückgewinnung.
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- Chemie Ingenieur Technik (CIT), 2000, v. 72, n. 9, p. 956, doi. 10.1002/1522-2640(200009)72:9<956::AID-CITE9560>3.0.CO;2-9
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Optimierung der HETP präparativer HPLC-Säulen.
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- Chemie Ingenieur Technik (CIT), 2000, v. 72, n. 5, p. 494, doi. 10.1002/1522-2640(200005)72:5<494::AID-CITE494>3.0.CO;2-W
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91. Dynamische Optimierung thermischer Trennverfahren.
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- Chemie Ingenieur Technik (CIT), 1998, v. 70, n. 9, p. 1130, doi. 10.1002/cite.330700993
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145. Einsatz von Simulation und Miniplants für die Entwicklung neuer Verfahrenskonzepte zur Trennung von Gemischen mit Mischungslücke.
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- Chemie Ingenieur Technik (CIT), 1998, v. 70, n. 9, p. 1174, doi. 10.1002/cite.3307009147
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- Article
180. Miniplanttechnik zur Koksofengasreinigung.
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- Chemie Ingenieur Technik (CIT), 1998, v. 70, n. 9, p. 1198, doi. 10.1002/cite.3307009182
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Auslegung von technischen Chromatographieanlagen.
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- Chemie Ingenieur Technik (CIT), 1997, v. 69, n. 9, p. 1219, doi. 10.1002/cite.330690904
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Flankierende Maßnahmen zur Einführung von 'Plantwide Control'︁-Konzepten.
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- Chemie Ingenieur Technik (CIT), 1997, v. 69, n. 9, p. 1329, doi. 10.1002/cite.3306909179
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P ROPER E DUCT (Process Operation - Education and Training): Eine offene Umgebung zur Schulung der Prozeßdynamik.
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- Chemie Ingenieur Technik (CIT), 1997, v. 69, n. 9, p. 1328, doi. 10.1002/cite.3306909178
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- Article
37. Modellgestützte Entwicklung einer zeitoptimalen Produktwechselstrategie für Rektifikationskolonnen.
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- Chemie Ingenieur Technik (CIT), 1996, v. 68, n. 9, p. 1086, doi. 10.1002/cite.330680939
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46. Zeitoptimale Produktwechselstrategien für Fraktionierkolonnen: Methodik, Vorgehensweise und Aufwand-/Nutzenanalyse.
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- Chemie Ingenieur Technik (CIT), 1994, v. 66, n. 9, p. 1190, doi. 10.1002/cite.330660947
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45. Entwicklung eines Beratungssystems zum Entwurf von Automatisierungskonzepten für Rektifikationskolonnen.
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- Chemie Ingenieur Technik (CIT), 1994, v. 66, n. 9, p. 1189, doi. 10.1002/cite.330660946
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72. Optimierung von Batch-Destillationsprozessen mit überlagerter chemischer Reaktion.
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- Chemie Ingenieur Technik (CIT), 1993, v. 65, n. 9, p. 1094, doi. 10.1002/cite.330650974
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78. Vergleich des dynamischen Verhaltens von Packungs- und Bodenrektifikationskolonnen.
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- Chemie Ingenieur Technik (CIT), 1993, v. 65, n. 9, p. 1097, doi. 10.1002/cite.330650980
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ASM3 extended for two-step nitrification-denitrification: a model reduction for sequencing batch reactors.
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- Journal of Chemical Technology & Biotechnology, 2012, v. 87, n. 7, p. 887, doi. 10.1002/jctb.3694
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Reaction engineering of oxidative coupling of methane: Experimental observations and analysis of the impacts of operating parameters.
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- Chemical Engineering Research & Design: Transactions of the Institution of Chemical Engineers Part A, 2021, v. 172, p. 84, doi. 10.1016/j.cherd.2021.04.029
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Methane oxidative coupling process for producing ethylene from fossil‐ and bio‐based methane.
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- Chemie Ingenieur Technik (CIT), 2018, v. 90, n. 9, p. 1135, doi. 10.1002/cite.201855007
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Eine robuste Prozessanalytik für die CO<sub>2</sub>-Abtrennung industrieller Gasströme basierend auf Online-NMR- und -Raman-Spektroskopie.
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- Chemie Ingenieur Technik (CIT), 2014, v. 86, n. 9, p. 1579, doi. 10.1002/cite.201450076
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Kontinuierliche Hydroformylierung von 1-Dodecen in wässrigen Mehrphasensystemen mit nichtionischen Tensiden.
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- Chemie Ingenieur Technik (CIT), 2014, v. 86, n. 9, p. 1507, doi. 10.1002/cite.201450078
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- Article