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56, 813-821, 2001. : Gas and liquid phase mass transfer within KATAPAK®-S structures studied using CFD simulations. Chem. Eng. , Vol. 57, 1531-1536, 2002. : Using computational fluid dynamics to calculate transversal dispersion in a structured packed bed. Comput. Chem. , Vol. 22, 767-770, 1998. : Liquid-phase mass transfer at low Reynolds number. Ind. Eng. Chem. , Vol. 2, 126-159, 1963. : Liquid mass transfer at very low Reynolds number in packed beds. Ind. Eng. Chem. , Vol. 5, 9-14, 1966. : Liquid holdup distribution in packed columns: gamma ray tomography and CFD simulation.

Eng. Chem. , Vol. 40, 6172-6180, 2001. : A corrugation geometry based model for efficiency of structured distillation packing. Chem. Eng. , Vol. 38, 683-695, 1999. : Multicomponent Mass Transfer in Packed Distillation Columns. PhD thesis, University of Dotmund, 1997. : Experimental Study on Multicomponent Distillation in Packed Columns. Chem. Eng. Process, Vol. 40, 235-243, 2001. : Pressure drop through structured packings: Breakdown into the contributing mechanisms by CFD modeling. Chem. Eng. , Vol.

40, 235-243, 2001. : Pressure drop through structured packings: Breakdown into the contributing mechanisms by CFD modeling. Chem. Eng. , Vol. 58, 163-177, 2003. : Vollständige Darstellung der turbulenten Geschwindigkeitsverteilung in glatten Leitungen. Z. angew. Math. , 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.

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