Order by: Author Year Journal Bibtex Type of Publication

{

• {Na Ranong}, C.;Hapke, J.;Fieg, G. (2020). Erratum to: Experimental investigation of exergy losses of a~PEM fuel cell system (Forschung im Ingenieurwesen, (2009), 73, 4, (193), 10.1007/s10010-009-0105-4). Forschung im Ingenieurwesen/Engineering Research. 84. (4), 387 [doi] [www]
  
  
• {Na Ranong}, C.;Hapke, J.;Fieg, G. (2009). Experimental investigation of exergy losses of a PEM fuel cell system. Forschung im Ingenieurwesen/Engineering Research. 73. (4), 193--203 [doi] [www]
  
  
• {Na Ranong}, C.;Höhne, M.;Franzen, J.;Hapke, J.;Fieg, G.;Dornheim, M.;Eigen, N.;{Bellosta Von Colbe}, J. M.;Metz, O. (2009). Concept, design and manufacture of a prototype hydrogen storage tank based on sodium alanate. Chemical Engineering and Technology. 32. (8), 1154--1163 [doi] [www]
  
  
• {Na Ranong}, C.;Lozano, G.;Hapke, J.;Roetzel, W.;Fieg, G.;{Bellosta Von Colbe}, J. M. (2011). Application of Danckwerts-type boundary conditions to the modeling of the thermal behavior of metal hydride reactors. Chemical Engineering Science. 66. (20), 4654--4662 [doi] [www]
  
  

A

• Ajmal, M.;Fieg, G. (2017). Intensification of Lipase-Catalyzed Esterification using Ultrasound: Process Engineering Perspectives. Chemie-Ingenieur-Technik. 89. (10), 1367--1373 [doi] [www]
  
  
• Ajmal, M.;Fieg, G.;Keil, F. (2016). Analysis of process intensification in enzyme catalyzed reactions using ultrasound. Chemical Engineering and Processing: Process Intensification. 110. 106--113 [doi] [www]
  
  
• Ajmal, M.;Rusli, S.;Fieg, G. (2016). Modeling and experimental validation of hydrodynamics in an ultrasonic batch reactor. Ultrasonics Sonochemistry. 28. 218--229 [doi] [www]
  
  

B

• Bohnenstädt, T.;Brandt, C.;Fieg, G.;Dietrich, W. (2014). Energy Integration Manager: A Workflow for Long Term Validity of Total Site Analysis and Heat Recovery Strategies. Computer Aided Chemical Engineering. 33. 1819--1824 [doi] [www]
  
  
• Bohnenstädt, T.;Fieg, G. (2014). A methodical approach for energy efficiency analysis based on existing process models. 21st International Congress of Chemical and Process Engineering, CHISA 2014 and 17th Conference on Process Integration, Modelling and Optimisation for Energy Saving and Pollution Reduction, PRES 2014. 4. [www]
  
  
• Bohnenstädt, T.;Fieg, G. (2014). A methodical approach for energy efficiency analysis based on existing process models. Chemical Engineering Transactions. 39. (Special Issue), 1411--1416 [doi] [www]
  
  
• Bohnenstädt, T.;Zimmermann, K.;Fieg, G. (2015). Optimisation of Process Parameters with Simultaneous Consideration of Energy Efficiency Measures. Computer Aided Chemical Engineering. 37. 749--754 [doi] [www]
  
  
• Brandt, C.;Fieg, G.;Luo, X. (2011). Efficient synthesis of heat exchanger networks combining heuristic approaches with a genetic algorithm. Heat and Mass Transfer/Waerme- und Stoffuebertragung. 47. (8), 1019--1026 [doi] [www]
  
  
• Brandt, C.;Fieg, G.;Luo, X.;Engel, O. (2012). New method for large-scale heat exchanger network synthesis. Computer Aided Chemical Engineering. 31. 695--699 [doi] [www]
  
  
• Buck, C.;Fieg, G. (2012). Platform for the design of process control structures of dividing wall columns [Entwicklungsplattform zum entwurf von prozessf’hrungskonzepten für trennwandkolonnen]. Chemie-Ingenieur-Technik. 84. (11), 2005--2013 [doi] [www]
  
  
• Buck, C.;Hiller, C.;Fieg, G. (2011). Applying Model Predictive Control to Dividing Wall Columns. Chemical Engineering and Technology. 34. (5), 663--672 [doi] [www]
  
  
• Buck, C.;Hiller, C.;Fieg, G. (2011). Decentralized temperature control of a pilot dividing wall column. Chemical Engineering and Processing: Process Intensification. 50. (2), 167--180 [doi] [www]
  
  

C

• Cai, K.;Guan, X.;Luo, X.;Fieg, G. (2009). Optimization of large-scale heat exchanger networks by evolution of sub-networks. Huagong Xuebao/CIESC Journal. 60. (9), 2265--2270 [www]
  
  

E

• Egger, L. S.;Fieg, G. (2017). Decentralized process control of reactive dividing wall columns. Chemical Engineering Transactions. 57. 1693--1698 [doi] [www]
  
  
• Egger, L. S.;Fieg, G. (2018). New process control concepts for energy efficient operation of reactive dividing wall columns. Chemical Engineering Transactions. 69. 541--546 [doi] [www]
  
  
• Egger, L. S.;Fieg, G. (2019). Process control for energy efficient operation of reactive dividing wall columns. Chemical Engineering Research and Design. 144. 397--404 [doi] [www]
  
  
• Egger, L. S.;Fieg, G. (2020). Experimental Investigation of Decentralized Process Control for Reactive Dividing-Wall Columns. Chemical Engineering and Technology. 43. (5), 964--973 [doi] [www]
  
  
• Egger, T.;Egger, L. S.;Fieg, G. (2018). Scale and causes of catalyst activity loss in enzymatic catalyzed reactive distillation. Chemical Engineering Science. 178. 324--334 [doi] [www]
  
  
• Egger, T.;Fieg, G. (2018). Dynamic process behavior and model validation of reactive dividing wall columns. Chemical Engineering Science. 179. 284--295 [doi] [www]
  
  
• Egger, T.;Fieg, G. (2017). Enzymatic catalyzed reactive dividing wall column: Experiments and model validation. AIChE Journal. 63. (6), 2198--2211 [doi] [www]
  
  
• Egger, T.;Fieg, G. (2019). Operation, validation and model comparison for a reactive dividing wall column. Chemical Engineering Science. 207. 993--1006 [doi] [www]
  
  
• Egger, T.;Hiller, C.;Fieg, G. (2018). Experimental Studies of a Petlyuk Column and Validation of a Non-Equilibrium Stage Model. Chemical Engineering and Technology. 41. (4), 827--835 [doi] [www]
  
  
• Ehlers, C.;Egger, T.;Fieg, G. (2017). Experimental operation of a reactive dividing wall column and comparison with simulation results. AIChE Journal. 63. (3), 1036--1050 [doi] [www]
  
  
• Ehlers, C.;Fieg, G. (2014). Experimental validation of a flexible modeling approach for distillation columns with packings. AIChE Journal. 60. (11), 3833--3847 [doi] [www]
  
  
• Ehlers, C.;Mohr, M.;Hiller, C.;Rix, A.;Fieg, G. (2016). Vorhersage der Trennleistung von FüllkÖrpern im Bereich der Rektifikation mit einem reduzierten Stofftransportansatz. Chemie-Ingenieur-Technik. 88. (9), 1283--1284 [doi] [www]
  
  
• Ehlers, C.;Schroeder, M.;Fieg, G. (2018). Solution to Lestak’s heat transfer problem for dividing wall columns and implications for practical operation. Chemical Engineering Transactions. 69. 463--468 [doi] [www]
  
  
• Ehlers, C.;Schröder, M.;Fieg, G. (2015). Influence of heat transfer across the wall of dividing wall columns on energy demand. AIChE Journal. 61. (5), 1648--1662 [doi] [www]
  
  
• Engelmann, C.;Ekambaram, N.;Johannsen, J.;Fellechner, O.;Waluga, T.;Fieg, G.;Liese, A.;Bubenheim, P. (2020). Enzyme Immobilization on Synthesized Nanoporous Silica Particles and their Application in a Bi-enzymatic Reaction. ChemCatChem. 12. (8), 2245--2252 [doi] [www]
  
  
• Engelmann, C.;Johannsen, J.;Waluga, T.;Fieg, G.;Liese, A.;Bubenheim, P. (2020). A multi-enzyme cascade for the production of highvalue aromatic compounds. Catalysts. 10. (10), 1--13 [doi] [www]
  
  
• Ernst, P.;Fieg, G.;Luo, X. (2010). Efficient synthesis of large-scale heat exchanger networks using monogenetic algorithm. Heat and Mass Transfer/Waerme- und Stoffuebertragung. 46. (10), 1087--1096 [doi] [www]
  
  
• Ernst, P.;Zimmermann, K.;Fieg, G. (2017). Multi-objective Optimization-Tool for the Universal Application in Chemical Process Design. Chemical Engineering and Technology. 40. (10), 1867--1875 [doi] [www]
  
  
• Ernst, P.;{Vargas Gomez}, M. A.;Fieg, G.;Luo, X. (2011). Hybrid method for the heat exchanger network synthesis [Método híbrido para la síntesis de una red de intercambiadores de calor]. Ingenieria Quimica (Spain). 43. (491), 70--73 [www]
  
  

F

• 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]
  
  
• 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. (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. (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.;Gao, Y.-M.;Luo, X. (2009). Modeling of separation process in a chromatographic column packed with porous adsorbents. Computer Aided Chemical Engineering. 26. 219--223 [doi] [www]
  
  
• 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]
  
  
• 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]
  
  
• 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. (1993). Sensitivitätsanalyse der Sprühtrocknung mittels eines Simulationsprogramms. Chemie Ingenieur Technik. 65. (11), 1372--1375 [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.;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]
  
  
• 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]
  
  
• Fieg, G.;{Temprano Martín}, M. (2002). Destilación batch con reflujo total. Ingenieria Quimica. 34. (392), 129 [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]
  
  

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]
  
  

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. (2018). Energy minimum design and systematic analysis of the reactive dividing wall column. Chemical Engineering Transactions. 69. 583--588 [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.;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]
  
  

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]
  
  

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]
  
  

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). 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. (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.;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-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]