Order by: Author Year Journal Bibtex Type of Publication

Z

• Zimmermann, K.;Fieg, G. (2017). Development of a Diversity-Preserving Strategy for the Pareto Optimization in Chemical Process Design. Chemie-Ingenieur-Technik. 89. (10), 1297--1305 [doi] [www]
  
  
• Zimmermann, K.;Fieg, G. (2018). Global Optimization of Superstructures and Decision Support via a universally applicable Optimization Tool. Computer Aided Chemical Engineering. 44. 763--768 [doi] [www]
  
  
• Zitzewitz, P.;Fieg, G. (2017). Multi-objective optimization superimposed model-based process design of an enzymatic hydrolysis process. AIChE Journal. 63. (6), 1974--1988 [doi] [www]
  
  
• Zitzewitz, P.;Fieg, G. (2014). New laboratory setup for the experimental analysis of a heterogeneous enzymatic hydrolysis with continuous liquid-liquid phase separation. Industrial and Engineering Chemistry Research. 53. (40), 15590--15599 [doi] [www]
  
  
• Zitzewitz, P.;Fieg, G. (2015). Holistic analysis of three-phasic enzymatic reaction systems using continuous liquid-liquid phase separation [Ganzheitliche Analyse dreiphasiger enzymatischer Reaktionssysteme mittels kontinuierlicher Flüssig-Flüssig-Phasentrennung]. Chemie-Ingenieur-Technik. 87. (6), 746--755 [doi] [www]
  
  

W

• Wozny, G.;Fieg, G.;Jeromin, L. (1989). Modellgestützte Kolonnenregelung. Chemie Ingenieur Technik. 61. (6), 488--489 [doi] [www]
  
  
• Wozny, G.;Fieg, G.;Jeromin, L.;Köhne, M.;Gülich, H. (1989). Design and analysis of a state observer for the temperature front of a retification column. Chemical Engineering & Technology. 12. (1), 339--344 [doi] [www]
  
  
• Wozny, G.;Fieg, G.;Kratz, G. (1988). Ermittlung der Automatisierungsstruktur von thermischen Trennprozessen. Chemie Ingenieur Technik. 60. (10), 788--789 [doi] [www]
  
  

V

• Vargas, M. A.;Fieg, G. (2012). Simulation study of alternatives for the efficient start-up of dividing-wall distillation column sequences. Computer Aided Chemical Engineering. 31. 750--754 [doi] [www]
  
  
• Vargas, M. A.;Niggemann, G.;Fieg, G. (2009). Dynamic modeling and simulation of dividing-wall distillation column systems. Computer Aided Chemical Engineering. 27. (C), 639--644 [doi] [www]
  
  

S

• Schneider, R.;Wozny, G.;Fieg, G. (1997). Investigations for process control strategies of a coupled, three-phase distillation plant with experimental verification. Institution of Chemical Engineers Symposium Series. (142 pt 1), [www]
  
  
• Schneider, R.;Wozny, G.;Fieg, G. (1997). Optimization of an industrial three phase distillation column train with experimental verification. Computers and Chemical Engineering. 21. (SUPPL.1), S1131-S1136 [doi] [www]
  
  
• Schröder, M.;Ehlers, C.;Fieg, G. (2016). A Comprehensive Analysis on the Reactive Dividing-Wall Column, its Minimum Energy Demand, and Energy-Saving Potential. Chemical Engineering and Technology. 39. (12), 2323--2338 [doi] [www]
  
  
• Schröder, M.;Fieg, G. (2016). Influence of Reaction System Properties on the Energy Saving Potential of the Reactive Dividing-Wall Column: Separation Properties. Chemical Engineering and Technology. 39. (12), 2265--2272 [doi] [www]
  
  
• Stegner, C.;Brandt, C.;Fieg, G. (2014). EVHE - A new method for the synthesis of HEN. Computers and Chemical Engineering. 64. 95--102 [doi] [www]
  
  

R

• Ranong, C. N.;Höhne, M.;Franzen, J.;Hapke, J.;Fieg, G.;Dornheim, M. (2009). Model supported process engineering calculation of a metal hydride storage based on sodium alanate on pilot scale [Modellgestützte verfahrenstechnische berechnung eines metallhydridspeichers auf natriumalanatbasis im technikumsmaßstab]. Chemie-Ingenieur-Technik. 81. (5), 645--654 [doi] [www]
  
  
• Ranong, C. N.;Maus, S.;Hapke, J.;Fieg, G.;Wenger, D. (2011). Approach for the determination of heat transfer coefficients for filling processes of pressure vessels with compressed gaseous media. Heat Transfer Engineering. 32. (2), 127--132 [doi] [www]
  
  
• Ratheins, M.;Fieg, G. (2018). Design of cost-optimal heat exchanger networks considering individual, match-dependent cost functions. 23rd International Congress of Chemical and Process Engineering, CHISA 2018 and 21st Conference on Process Integration, Modelling and Optimisation for Energy Saving and Pollution Reduction, PRES 2018. 2. [www]
  
  
• Rathjens, M.;Bohnenstädt, T.;Fieg, G.;Engel, O. (2016). Synthesis of Heat Exchanger Networks Taking into Account Cost and Dynamic Considerations. Procedia Engineering. 157. [doi] [www]
  
  
• Rathjens, M.;Fieg, G. (2018). Design of cost-optimal heat exchanger networks considering individual, match-dependent cost functions. Chemical Engineering Transactions. 70. 601--606 [doi] [www]
  
  
• Rathjens, M.;Fieg, G. (2019). Cost-optimal heat exchanger network synthesis based on a flexible cost functions framework. Energies. 12. (5), [doi] [www]
  
  
• Rathjens, M.;Fieg, G. (2020). A novel hybrid strategy for cost-optimal heat exchanger network synthesis suited for large-scale problems. Applied Thermal Engineering. 167. [doi] [www]
  
  
• Rave, A.;Kuwertz, R.;Fieg, G.;Heck, J. (2019). Characterization of a Modular, Scalable Millistructured Plate Reactor. Chemie-Ingenieur-Technik. 91. (5), 602--606 [doi] [www]
  
  
• Rave, A.;Kuwertz, R.;Fieg, G.;Heck, J. (2020). Modeling and experimental investigation of the spatial heat transfer in a plate reactor with meandering millichannels. Chemical Engineering and Processing - Process Intensification. 150. [doi] [www]
  
  
• Remberg, C.;Fett, F. N.;Wozny, G.;Fieg, G.;Blaich, L. (1995). Entwicklung eines Beratungssystems zum Entwurf von Automatisierungskonzepten für Rektifikationskolonnen. Chemie Ingenieur Technik. 67. (7), 866--870 [doi] [www]
  
  
• Roetzel, W.;{Na Ranong}, C.;Fieg, G. (2011). New axial dispersion model for heat exchanger design. Heat and Mass Transfer/Waerme- und Stoffuebertragung. 47. (8), 1009--1017 [doi] [www]
  
  

N

• Neidert, M.;Fieg, G.;Ridinger, R. (1998). BatchMan - Ein anwendungsorientiertes Softwareprodukt zur Analyse von Batchprozessen. Chemie-Ingenieur-Technik. 70. (7), 846--849 [doi] [www]
  
  
• Niggemann, G.;Fieg, G. (2012). Validation of dividing-wall columns based on experimental data and dynamic simulations: Pilot-plant and production-scale columns. Industrial and Engineering Chemistry Research. 51. (2), 931--943 [doi] [www]
  
  
• Niggemann, G.;Fieg, G.;de {La Torre Díaz}, M.;Luo, X. (2009). Start of a divided wall distillation column: Modeling and simulation of hydraulic performance [Arranque de una columna de destilación de pared dividida: Modelado y simulación del comportamiento hidráulico]. Ingenieria Quimica (Spain). 41. (470), 110--115 [www]
  
  
• Niggemann, G.;Hiller, C.;Fieg, G. (2010). Experimental and theoretical studies of a dividing-wall column used for the recovery of high-purity product (Industrial and Engineering Chemistry Research 49:14 (6570)). Industrial and Engineering Chemistry Research. 49. (23), 12331 [doi] [www]
  
  
• Niggemann, G.;Hiller, C.;Fieg, G. (2010). Experimental and Theoretical Studies of a Dividing-Wall Column Used for the Recovery of High-Purity Products. Industrial and Engineering Chemistry Research. 49. (14), 6566--6577 [doi] [www]
  
  
• Niggemann, G.;Hiller, C.;Fieg, G. (2011). Modeling and in-depth analysis of the start-up of dividing-wall columns. Chemical Engineering Science. 66. (21), 5268--5283 [doi] [www]
  
  
• Numrich, R.;Möller, K.;Fieg, G. (1996). Simulation eines industriellen Fallfilmverdampfers zur Verdampfung von Mehrstoffgemischen. Chemie-Ingenieur-Technik. 68. (11), 1466--1469 [doi] [www]
  
  

M

• Meyer, F.;Johannsen, J.;Liese, A.;Fieg, G.;Bubenheim, P.;Waluga, T. (2021). Evaluation of process integration for the intensification of a biotechnological process. Chemical Engineering and Processing - Process Intensification. 108506 [doi]
  
  

L

• Lange, A. and Fieg, G. (2022). Designing Novel Structured Packings by Topology Optimization and Additive Manufacturing. 49. 1291--1296 [doi]
  
  
• Lawen, J.;Yu, H.;Fieg, G.;Abdel-Wahab, A. (2013). New unstructured mesh water quality model for coastal discharges. Environmental Modelling and Software. 40. 330--335 [doi] [www]
  
  
• Lawen, J.;Yu, H.;Fieg, G.;Abdel-Wahab, A.;Bhatelia, T. (2014). New Unstructured Mesh Water Quality Model for Cooling Water Biocide Discharges. Environmental Modeling and Assessment. 19. (1), 1--17 [doi] [www]
  
  
• Leipold, M.;Fieg, G. (2011). Enzymatically catalyzed fixed bed reactions - Modeling and simulation [Enzymatisch katalysierte reaktionen im festbettreaktor - modellierung und simulation]. Chemie-Ingenieur-Technik. 83. (3), 340--348 [doi] [www]
  
  
• Leipold, M.;Gruetzmann, S.;Fieg, G. (2009). Model based optimisation of the design of a middle vessel batch distillation by using an evolutionary algorithm [Modellgestützte optimierung des designs einer batch-rektifikation mit mittelbehälter mittels eines evolutionären algorithmus]. Forschung im Ingenieurwesen/Engineering Research. 73. (3), 161--172 [doi] [www]
  
  
• Leipold, M.;Gruetzmann, S.;Fieg, G. (2009). An evolutionary approach for multi-objective dynamic optimization applied to middle vessel batch distillation. Computers and Chemical Engineering. 33. (4), 857--870 [doi] [www]
  
  
• Leipold, M.;Gruetzmann, S.;Fieg, G.;Maschmeyer, D.;Sauer, J.;Wiederhold, H. (2008). Development of a sophisticated framework for complex single-and multi-objective optimization tasks. Computer Aided Chemical Engineering. 25. 695--700 [doi] [www]
  
  
• Leipold, M.;Gruetzmann, S.;{Vargas Gomez}, M. A.;Fieg, G.;Luo, X. (2010). Optimal design of a batch distillation column with cyclic product collection [Diseño óptimo de una columna de destilación batch con recogida cíclica de productos]. Ingenieria Quimica (Spain). 42. (478), 144--151 [www]
  
  
• Liang, J.;Fieg, G. (2013). A combination of experiments and molecular dynamics simulation for the investigation of the ion-exchange adsorption of biological macromolecules. Computer Aided Chemical Engineering. 32. 25--30 [doi] [www]
  
  
• Liang, J.;Fieg, G.;Jakobtorweihen, S. (2015). Molecular Dynamics Simulations of a Binary Protein Mixture Adsorption onto Ion-Exchange Adsorbent. Industrial and Engineering Chemistry Research. 54. (10), 2794--2802 [doi] [www]
  
  
• Liang, J.;Fieg, G.;Jakobtorweihen, S. (2015). Ion-Exchange Adsorption of Proteins: Experiments and Molecular Dynamics Simulations. Chemie-Ingenieur-Technik. 87. (7), 903--909 [doi] [www]
  
  
• Liang, J.;Fieg, G.;Jakobtorweihen, S. (2014). Molecular dynamics simulations of competitive protein adsorption onto chromatographic media. Computer Aided Chemical Engineering. 33. 937--942 [doi] [www]
  
  
• Liang, J.;Fieg, G.;Keil, F. J.;Jakobtorweihen, S. (2012). Adsorption of proteins onto ion-exchange chromatographic media: A molecular dynamics study. Industrial and Engineering Chemistry Research. 51. (49), 16049--16058 [doi] [www]
  
  
• Liang, J.;Fieg, G.;Shi, Q.-H.;Sun, Y. (2012). Single and binary adsorption of proteins on ion-exchange adsorbent: The effectiveness of isothermal models. Journal of Separation Science. 35. (17), 2162--2173 [doi] [www]
  
  
• Liang-Schenkelberg, J.;Fieg, G.;Waluga, T. (2017). Molecular Insight into Affinity Interaction between Cibacron Blue and Proteins. Industrial and Engineering Chemistry Research. 56. (34), 9691--9697 [doi] [www]
  
  
• Lozano, G. A.;Ranong, C. N.;von Colbe, J.M.B.;Bormann, R.;Fieg, G.;Hapke, J.;Dornheim, M. (2010). Empirical kinetic model of sodium alanate reacting system (I). Hydrogen absorption. International Journal of Hydrogen Energy. 35. (13), 6763--6772 [doi] [www]
  
  
• Lozano, G. A.;Ranong, C. N.;{Bellosta Von Colbe}, J. M.;Bormann, R.;Fieg, G.;Hapke, J.;Dornheim, M. (2010). Empirical kinetic model of sodium alanate reacting system (II). Hydrogen desorption. International Journal of Hydrogen Energy. 35. (14), 7539--7546 [doi] [www]
  
  
• Lozano, G. A.;Ranong, C. N.;{Bellosta Von Colbe}, J. M.;Bormann, R.;Hapke, J.;Fieg, G.;Klassen, T.;Dornheim, M. (2012). Optimization of hydrogen storage tubular tanks based on light weight hydrides. International Journal of Hydrogen Energy. 37. (3), 2825--2834 [doi] [www]
  
  
• Luder, T.;Wozny, G.;Fieg, G.;Jeromin, L. (1990). Model based observations and control of distillation columns. [www]
  
  
• Luo, X.;Fieg, G.;Cai, K.;Guan, X. (2009). Synthesis of large-scale heat exchanger networks by a monosenetic algorithm. Computer Aided Chemical Engineering. 27. (C), 729--734 [doi] [www]
  
  
• Luo, X.;Wen, Q.-Y.;Fieg, G. (2009). A hybrid genetic algorithm for synthesis of heat exchanger networks. Computers and Chemical Engineering. 33. (6), 1169--1181 [doi] [www]
  
  

K

• Kao, Y.-L.;Fieg, G.;Ward, J. D. (2017). Closed Operation of Multivessel Batch Reactive Distillation Processes. Industrial and Engineering Chemistry Research. 56. (13), 3655--3670 [doi] [www]
  
  
• Krause, P.;Fieg, G. (2011). Experiment based model development for the enzymatic hydrolysis in a packed-bed reactor with biphasic reactant flow. Chemical Engineering Science. 66. (20), 4838--4850 [doi] [www]
  
  
• Krause, P.;Fieg, G. (2012). Applicability of a simple laboratory setup for the extractive hydrolysis using immobilized enzymes. Chemical Engineering and Processing: Process Intensification. 60. 77--85 [doi] [www]
  
  
• Krause, P.;Fieg, G. (2012). Influence of the organic phase fraction in the biphasic organic-aqueous reactor feed stream on the enzymatic hydrolysis of FAME in a packed bed. Computer Aided Chemical Engineering. 31. 730--734 [doi] [www]
  
  
• Krause, P.;Hilterhaus, L.;Fieg, G.;Liese, A.;Bornscheuer, U. (2009). Chemically and enzymatically catalyzed synthesis of C6-C10 alkyl benzoates. European Journal of Lipid Science and Technology. 111. (2), 194--201 [doi] [www]
  
  
• Krause, P.;MacIas, R.;Fieg, G. (2010). Applicability of a countercurrent enzymatically catalyzed multistage extractive reaction process for the hydrolysis of methyl octanoate. Industrial and Engineering Chemistry Research. 49. (7), 3217--3222 [doi] [www]
  
  
• Krause, P.;MacIas, R.;Fieg, G.;Gutsche, B. (2009). Method for determination of the reaction kinetics of an enzymatic conversion in a heterogeneous system. Computer Aided Chemical Engineering. 26. 1081--1085 [doi] [www]
  
  
• Kruse, C.;Fieg, G.;Wozny, G. (1995). Development and experimental verification of a simulation tool for distillation column startup [Entwicklung und experimentelle Absicherung eines Simulationsprogrammes für Anfahrvorgänge an Rektifikationskolonnen]. Heat and Mass Transfer. 31. (1-2), 25--31 [doi] [www]
  
  
• Kruse, C.;Fieg, G.;Wozny, G.;Jeromin, L. (1995). Algorithmus zur Reduzierung des Zeitbedarfs bei Anfahrvorgängen an Rektifikationskolonnen. Chemie Ingenieur Technik. 67. (4), 458--461 [doi] [www]
  
  
• Kruse, C.;Fieg, G.;Wozny, G.;Jeromin, L.;Johannisbauer, W. (1995). Experimental Verification of the Equilibrium Stage Model for the Dynamics of the Multicomponent Distillation Considering the Effects of Energy Loss. Industrial and Engineering Chemistry Research. 34. (5), 1810--1822 [doi] [www]
  
  
• Kruse, Ch.;Fieg, G.;Wozny, G. (1996). A new time-optimal strategy for column startup and product changeover. Journal of Process Control. 6. (2-3 SPEC. ISS), 187--193 [doi] [www]
  
  
• Kruse, Ch.;Fieg, G.;Wozny, G.;Jeromin, L. (1995). Industrial realization of time-optimal strategies for product changeover operations of coupled distillation columns. Computers and Chemical Engineering. 19. (SUPPL. 1), 603--608 [doi] [www]
  
  

J

• Johannsen, J.;Baek, G.;Fieg, G.;Waluga, T. (2021). An innovative approach for fatty acid reduction to fatty aldehydes. Green Chemistry Letters and Reviews. 14. (3), 454--460 [doi]
  
  
• Johannsen, J.;Engelmann, C.;Liese, A.;Fieg, G.;Bubenheim, P.;Waluga, T. (2020). Pilot-scale operation of a multi-enzymatic cascade reaction in a multiphase system. Chemical Engineering Transactions. 79. 25--30 [doi] [www]
  
  
• Johannsen, J.;Meyer, F.;Engelmann, C.;Liese, A.;Fieg, G.;Bubenheim, P.;Waluga, T. (2021). Multi-enzyme cascade reaction in a miniplant two-phase-system: Model validation and mathematical optimization. AIChE Journal. [doi]
  
  
• Johannsen, J.;Meyer, F.;Fieg, G.;Waluga, T. (2020). Process for the Preparation of Fatty Aldehydes from Renewable Resources. Chemie-Ingenieur-Technik. 92. (6), 777--781 [doi] [www]
  
  
• Josten, H.;Fieg, G.;Gutsche, B.;Johannisbauer, W. (2004). Urea precipitation as a competitive separation process for difficult separations in oleochemistry [Harnstofffällung als konkurrenzfähiges Trennverfahren für schwierige Stofftrennungen in der Oleochemie]. Chemie-Ingenieur-Technik. 76. (11), 1700--1703 [doi] [www]
  
  

H

• Hagedorn, A.;Fieg, G.;Winter, D.;Koschikowski, J.;Grabowski, A.;Mann, T. (2017). Membrane and spacer evaluation with respect to future module design in membrane distillation. Desalination. 413. 154--167 [doi] [www]
  
  
• Hagedorn, A.;Fieg, G.;Winter, D.;Koschikowski, J.;Mann, T. (2017). Methodical design and operation of membrane distillation plants for desalination. Chemical Engineering Research and Design. 125. 265--281 [doi] [www]
  
  
• Harding, L.-S.;Fieg, G. (2020). Energy saving potential of reactive dividing wall columns with azeotropic reaction systems. Chemical Engineering Science. 227. [doi] [www]
  
  
• Harding, L.-S.;Fieg, G. (2018). Energy minimum design and systematic analysis of the reactive dividing wall column. Chemical Engineering Transactions. 69. 583--588 [doi] [www]
  
  
• Harding, L.-S.;Schroeder, M.;Fieg, G. (2018). Hybrid Global Optimization Method for the Analysis of Integrated Reaction and Separation Processes. Computer Aided Chemical Engineering. 44. 1027--1032 [doi] [www]
  
  
• Hartig, D.;Waluga, T.;Schmidt, C.;Fieg, G.;Scholl, S. (2017). Extended Elution by Characteristic Point Method for Characterization of Protein Ion-Exchange Adsorption. Chemical Engineering and Technology. 40. (10), 1940--1945 [doi] [www]
  
  
• Hiller, C.;Buck, C.;Ehlers, C.;Fieg, G. (2010). Nonequilibrium stage modelling of dividing wall columns and experimental validation. Heat and Mass Transfer/Waerme- und Stoffuebertragung. 46. (10), 1209--1220 [doi] [www]
  
  
• Horsch, A. S. and Hamann, D. and Egger, L. S. and Fieg, G. and Skiborowski, M. (2022). Demonstration of applied linear model predictive control for an enzymatic reactive dividing wall column. Chemical Engineering Research and Design. 178. 251--266 [doi]
  
  
• Horsch, A. S.;Egger, L. S.;Fieg, G. (2020). Linear Model Predictive Control for a Reactive Dividing Wall Column. European Control Conference 2020, ECC 2020. [www]
  
  

G

• Gruetzmann, S.;Fieg, G. (2006). Improvements in configuration of a middle vessel batch distillation by means of rigorous dynamic modelling and simulation. Proceedings of the 15th IASTED International Conference on Applied Simulation and Modelling. 2006. [www]
  
  
• Gruetzmann, S.;Fieg, G. (2007). Integrale Analyse der Batch-rektifikation mit Mittelbehälter. Chemie-Ingenieur-Technik. 79. (10), 1613--1624 [doi] [www]
  
  
• Gruetzmann, S.;Fieg, G. (2008). Startup operation of middle-vessel batch distillation column: Modeling and simulation. Industrial and Engineering Chemistry Research. 47. (3), 813--824 [doi] [www]
  
  
• Gruetzmann, S.;Fieg, G.;Kapala, T. (2006). Theoretical analysis and operating behaviour of a middle vessel batch distillation with cyclic operation. Chemical Engineering and Processing: Process Intensification. 45. (1), 46--54 [doi] [www]
  
  
• Gruetzmann, S.;Fieg, G.;Skogestad, S. (2009). Experimental and theoretical studies on the start-up operation of a multivessel batch distillation column. Industrial and Engineering Chemistry Research. 48. (11), 5336--5343 [doi] [www]
  
  
• Gruetzmann, S.;Kapala, T.;Fieg, G. (2006). Dynamic modelling of complex batch distillation starting from ambient conditions. Computer Aided Chemical Engineering. 21. (C), 865--870 [doi] [www]
  
  
• Gruetzmann, S.;Temprano, M.;Kapala, T.;Fieg, G. (2005). Command concepts to minimize the process time of cyclic batch rectification [Führungskonzepte zur Minimierung der Prozessdauer der zyklischen Batch-Rektifikation]. Chemie-Ingenieur-Technik. 77. (8), 1101--1102 [doi] [www]
  
  

F

• Fieg, G.;Gutermuth, W.;Kothe, W.;Mayer, H. H.;Nagel, S.;Wendeler, H.;Wozny, G. (1995). A standard interface for use of thermodynamics in process simulation. Computers and Chemical Engineering. 19. (SUPPL. 1), 317--320 [doi] [www]
  
  
• Fieg, G.;Gutermuth, W.;Kothe, W.;Mayer, H.?H.;Nagel, S.;Wendeler, H.;Wozny, G. (1995). Programmierrichtlinien FORTRAN und C der IK?CAPE. Chemie Ingenieur Technik. 67. (4), 479--481 [doi] [www]
  
  
• Fieg, G.;Hou, X.-R.;Luo, X.;Ma, H.-G. (2009). The optimal design of heat exchanger networks considering heat exchanger types. Computer Aided Chemical Engineering. 26. 659--664 [doi] [www]
  
  
• Fieg, G.;Landwehr, B.;Wozny, G. (1996). About the possibility of a direct concentration control for distillation columns. Chemical Engineering and Technology. 19. (4), 299--307 [doi] [www]
  
  
• Fieg, G.;Luo, X.;Jezowski, J. (2009). A monogenetic algorithm for optimal design of large-scale heat exchanger networks. Chemical Engineering and Processing: Process Intensification. 48. (11-12), 1506--1516 [doi] [www]
  
  
• Fieg, G.;Wozny, G.;Buick, K.;Jeromin, L. (1994). Estimation of the drying rate and moisture profiles in an industrial spray dryer by means of experimental investigations and a simulation study. Chemical Engineering & Technology. 17. (4), 235--241 [doi] [www]
  
  
• Fieg, G.;Wozny, G.;Buick, K.;Jeromin, L. (1993). Sensitivitätsanalyse der Sprühtrocknung mittels eines Simulationsprogramms. Chemie Ingenieur Technik. 65. (11), 1372--1375 [doi] [www]
  
  
• Fieg, G.;Wozny, G.;Jeromin, L. (1992). Design, analysis and realization of a state control system for an industrial distillation column. Journal of Process Control. 2. (4), 179--187 [doi] [www]
  
  
• Fieg, G.;Wozny, G.;Jeromin, L. (1992). Experimental and theoretical studies of the steady-state and dynamic behaviour of packed columns. Chemical Engineering and Processing. 31. (6), 377--383 [doi] [www]
  
  
• Fieg, G.;Wozny, G.;Jeromin, L.;Kruse, C. (1994). Comparison of the dynamic behaviour of packed and plate distillation columns. Chemical Engineering & Technology. 17. (5), 301--306 [doi] [www]
  
  
• Fieg, G.;Wozny, G.;Kruse, Chr. (1993). Experimental and theoretical studies of the dynamics of startup and product switchover operations of distillation columns. Chemical Engineering and Processing. 32. (5), 283--290 [doi] [www]
  
  
• Flender, M.;Fieg, G.;Wozny, G. (1996). Classification of New Product changeover Strategy (NPS) for different application of distillation columns. Computers and Chemical Engineering. 20. (SUPPL.2), S1131-S1136 [doi] [www]