By Kenig E.Y.

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Vol. 31, 208-219, 1951. Reynolds A. : Turbulent Flows in Engineering. Wiley, New York 1974. : Distillation columns containing structured packings: A comprehensive model for their performance. 1. Hydraulic models. Ind. Eng. Chem. , Vol. 32, 641-651, 1993. : Grenzschicht-Theorie. Springer, Berlin, 1997. , Górak, A. ): Integrated Reaction and Separation Operations. Modelling and experimental validation. Springer, Berlin, 2006. : The rate-based approach for modelling staged separations. Chem. Eng.

Seidel-Morgenstern, A. : Integrated Chemical Processes: Synthesis, Operation, Analysis, and Control. Wiley-VCH, Weinheim, 2005. : Multicomponent Mass Transfer. Wiley, New York, 1993. : Micro-engineered catalyst systems: ABB's advancement in structured catalytic packings. Catal. Today, Vol. 69, 17-24, 2001. Published by The Berkeley Electronic Press, 2007 29 Chemical Product and Process Modeling, Vol. 2 [2007], Iss. 1, Art. : Mikrodestillation von Mehrkomponentensystemen. Chem. Ing. , Vol. 68, 272-276, 1996.

Springer, Berlin, 1997. , Górak, A. ): Integrated Reaction and Separation Operations. Modelling and experimental validation. Springer, Berlin, 2006. : The rate-based approach for modelling staged separations. Chem. Eng. , Vol. 85, Nr. 10, 41-49, 1989. : Mass Transfer. McGraw-Hill, New York, 1975. : Application of the hydrodynamic analogy approach to the modelling of structured-packing-containing columns. Proc. PRES’05 -8th Conference on Process Integration, Modelling and Optimisation for Energy Saving and Pollution Reduction, Giardini Naxos, 2005a.

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