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European Congress of Chemical Engineering - 6
Copenhagen 16-21 September 2007

Abstract 3539 - Mathematical modelling of multicomponent transport in silicalite-1/α-alumina membrane

Mathematical modelling of multicomponent transport in silicalite-1/α-alumina membrane

Advancing the chemical engineering fundamentals

Membranes and Membrane Science - I (T2-8a)

Dr Vlastimil Fila
Institute od Chemical Technology
Department of Inorganic Technology
Technicka 5
166 29 Prague 6
Czech Republic

Asc. Prof Bohumil Bernauer
Institute of Chemical Technology, Prague
Department of Inorganic Technology
Technicka 5
166 28 Prague 6
Czech Republic

Dr Milan Kocirik
Academy of Sciences of the Czech Republic
J. Heyrovsky Institute of Physical Chemistry
Dolejskova 3
18223 Prague 8
Czech Republic

Dr Arlette Zikanova
Academy of Sciences of the Czech Republic
J. Heyrovsky Institute of Physical Chemistry
Dolejskova 3
18223 Prague 8
Czech Republic

Mr Pavel Hrabanek
Academy of Sciences of the Czech Republic
J. Heyrovský Institute of Physical Chemistry
Dolejškova 3
182 23 Prague 8
Czech Republic

Ing Vladimir Navara
Institute of Chemical Technology Prague
Department of Inorganic Technology
Technicka 5
16628 Prague 6
Czech Republic

Keywords: silicalite-1, membrane, modelling, semi-open W-K cell, separation

Composite ceramic-zeolite membranes are promising candidates for various separation and catalytic processes. Ceramic-zeolite tailor-made separation membranes could provide i) selective separations of various gas mixtures in industrially important applications (e.g. n-butane/isobutane separation), ii) selective separative pore wall allowing to overcome the thermodynamic limits of the reactant conversion in membrane reactors. In this respect, synthesis and characterization of ceramic-zeolite membranes with evaluation of structural, permeation and separation properties is widely studied by many authors.
The present study is mainly focused on mass transport modelling through composite silicalite-1/a-alumina membranes and support contribution to overall mass transport and separation of prepared membranes.
Overall transport properties of a membrane are determined by number and nature of defects as well as textural properties of a support. Pore size distribution of support and interaction of pore surface with permeating species determine transport, which effects species composition on zeolite layer/support interface and consequently separation efficiency of a composite membrane.
The dynamic permeations of binary mixtures and single components in a semi-open Wicke-Kallenbach cell were used to measure total pressure difference and gas mixture composition in a closed compartment. These data were treated by a mathematical model based on Dusty-gas and Maxwell-Stefan-Krishna theory where the effects of support layer were taken into account during calculations. Resulting system of PDEs, ODEs and AEs is solved by a home-made general simulation FORTRAN program that is based on a method of lines with collocation differentiation in spatial coordinate. The textural and transport parameters were estimated by a multi-response regression method.

The financial support of this research by the Grant Agency of the ASCR under project number 1QS401250509 and by the Ministry of Education, Youth and Sports under project number MSM 604 613 73 01 is gratefully acknowledged.

Presented Tuesday 18, 16:20 to 16:40, in session Membranes and Membrane Science - I (T2-8a).

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