A POD-ROM Methodology for optimal structuring of a non-isothermal fixed-bed reactor for process integration / Katarzyna Bizon, Gaetano Continillo, Enrico A. Cutillo, Alfonso D’Onofrio // W: 31st European ... więcej

A POD-ROM Methodology for optimal structuring of a non-isothermal fixed-bed reactor for process integration / Katarzyna Bizon, Gaetano Continillo, Enrico A. Cutillo, Alfonso D’Onofrio // W: 31st European Symposium on Computer Aided Process Engineering : ESCAPE-31 [Dokument elektroniczny] / ed. by Metin Türkay, Rafiqul Gani. – Amsterdam [etc.] : Elsevier, 2021. – (Computer Aided Chemical Engineering, ISSN 1570-7946 ; Vol. 50). – S. 307-312 : wykr. – Tryb dostępu: https://www.sciencedirect.com/science/article/pii/B9780323885065500498. – Bibliogr. 7 poz., Abstr. – Mat. konf.: ESCAPE-31, Istanbul, Turkey (konferencja online), 6-9.06.2021. – doi: 10.1016/B978-0-323-88506-5.50049-8. – ISBN 978-0-323-88506-5

The structure of a catalytic reactor integrating two reactions is yield-optimized in terms of distribution of active sites of two catalysts in a hybrid pellet, using a two-scale (pellet and reactor) approach. ... więcej

The structure of a catalytic reactor integrating two reactions is yield-optimized in terms of distribution of active sites of two catalysts in a hybrid pellet, using a two-scale (pellet and reactor) approach. POD-Galërkin model reduction is adopted to reduce the burden of the optimization algorithm. Results show that optimal structuring can have a key role in catalyst process intensification, in terms of yield, chosen as the performance indicator and thus also as the objective function for the optimization problem.