Prof. Dr.-Ing. Georg Fieg

(former head of the Institute for Process and Plant Engineering)

Am Schwarzenberg-Campus 4 (C)

21073 Hamburg

Building: C - Room: 1.003

eMail: Prof.-Dr. Fieg

Phone: ++49 (0)40 42878-6111

  • Modelling and simulation of complex process engineering processes
  • Methods of single- and multi-criteria process optimization
  • Development and experimental testing of novel process control concepts
  • Modelling and simulation of fixed-bed reactors with carrier-fixed enzymes
  • Synthesis, design and construction of hydrogen storage systems based on metal hydride
  • Optimisation of heat exchanger networks

2009

  • 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]

  • 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]

  • 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]

  • 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]

2008

  • 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]

  • 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]

2007

  • Fieg, G.;{Temprano Martín}, M. (2007). Automatic exit control of rectification columns [Control de salidas para la operación automática de columnas de rectificación]. Ingenieria Quimica. 39. (445), 154--158 [www]

  • Gruetzmann, S.;Fieg, G. (2007). Integrale Analyse der Batch-rektifikation mit Mittelbehälter. Chemie-Ingenieur-Technik. 79. (10), 1613--1624 [doi] [www]

2006

  • 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.;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.;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]

2005

  • Fieg, G. (2005). Design and analysis of an integral startup system for distillation columns. Chemical Engineering Research and Design. 83. (5 A), 445--451 [doi] [www]

  • Fieg, G.;Gruetzmann, S.;Temprano, M.;Kapala, T. (2005). Experimental investigation of batch distillation with reduced cycling of the products [Investigación experimental de la destilación batch con disminución cíclica de productos]. Ingenieria Quimica. 37. (429), 90--97 [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]

2004

  • Fieg, G.;Gruetzmann, S. (2004). An optimal startup procedure for industrial distillation columns: Development strategy and experimental validation. Inzynieria Chemiczna i Procesowa. 25. (3 I), 855--858 [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]

2002

  • Fieg, G. (2002). Composition control of distillation columns with a sidestream by using gas chromatographs. Chemical Engineering and Processing. 41. (2), 123--133 [doi] [www]

  • Fieg, G.;{Temprano Martín}, M. (2002). Destilación batch con reflujo total. Ingenieria Quimica. 34. (392), 129 [www]

1998

  • Neidert, M.;Fieg, G.;Ridinger, R. (1998). BatchMan - Ein anwendungsorientiertes Softwareprodukt zur Analyse von Batchprozessen. Chemie-Ingenieur-Technik. 70. (7), 846--849 [doi] [www]

1997

  • 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]

1996

  • Fieg, G. (1996). Some aspects of the dynamic simulation of mass separation apparatus with respect to its transferability to real plants [Einige Aspekte der dynamischen Simulation von Stofftrennapparaten im Hinblick auf ihre Übertragung auf reale Anlagen]. Heat and Mass Transfer/Waerme- und Stoffuebertragung. 31. (4), 205--213 [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]

  • 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]

  • 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]

  • Numrich, R.;Möller, K.;Fieg, G. (1996). Simulation eines industriellen Fallfilmverdampfers zur Verdampfung von Mehrstoffgemischen. Chemie-Ingenieur-Technik. 68. (11), 1466--1469 [doi] [www]

1995

  • 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]

  • 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.;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]

  • 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]

1994

  • 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.;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]

1993

  • 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.;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]

1992

  • 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]

1990

  • Luder, T.;Wozny, G.;Fieg, G.;Jeromin, L. (1990). Model based observations and control of distillation columns. [www]

1989

  • 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]

1988

  • Wozny, G.;Fieg, G.;Kratz, G. (1988). Ermittlung der Automatisierungsstruktur von thermischen Trennprozessen. Chemie Ingenieur Technik. 60. (10), 788--789 [doi] [www]

1976

  • Fieg, G. (1976). EXPERIMENTAL INVESTIGATIONS OF HEAT TRANSFER CHARACTERISTICS IN LIQUID LAYERS WITH INTERNAL HEAT SOURCES. Proc of the Int Meet on Fast React Saf and Relat Phys. 4. 2047--2055 [www]

12

weitere Veröffentlichungen

Konferenzbeiträge Prof. Dr.-Ing. Georg Fieg