Networks of catalytic reactors with periodically switched inlet and outlet sections offer a competitive technological solution to the operation of reversible exothermic reactions. Traditionally, this operation mode is implemented by periodically shifting inlet and outlet sections so as to jump a single reactor unit in the flow direction. Here, a network of four catalytic reactors carrying on the methanol synthesis process is considered and the effect of varying the number (n s) of reactor units jumped by inlet and outlet sections on network stability and performance is investigated. Increasing n s, a greater variety of periodic regimes giving rise to trains of temperature waves characterized by spatial periodicity are detected as the switching velocity varies. These regimes well reproduce the inter-stage cooling effect of multistage fixed bed reactors and, hence, guarantee in general large conversion values. Moreover, an intriguing coexistence between T-periodic and multi-periodic temperature wave trains is revealed, T being the period needed for the system to recover its initial configuration. A T-periodic symmetric wave train characterized by k waves always coexists with a number of k-1 stable symmetric kT-periodic regimes, except when symmetry breaking is encountered. The k-1 coexisting regimes correspond to wave trains with a number of waves ranging between 1 and k-1. Bifurcational analysis is performed to characterize the stability range of periodic regimes and to systematically analyze multiplicities and bifurcations as the switching velocity is varied and at different n s. © 2011 Elsevier B.V.

Multiplicities of temperature wave trains in periodically forced networks of catalytic reactors for reversible exothermic reactions / Erasmo, Mancusi; Altimari, Pietro; Lucia, Russo; Crescitelli, Silvestro. - In: CHEMICAL ENGINEERING JOURNAL. - ISSN 1385-8947. - STAMPA. - 171:2(2011), pp. 655-668. [10.1016/j.cej.2011.04.026]

Multiplicities of temperature wave trains in periodically forced networks of catalytic reactors for reversible exothermic reactions

ALTIMARI, PIETRO;
2011

Abstract

Networks of catalytic reactors with periodically switched inlet and outlet sections offer a competitive technological solution to the operation of reversible exothermic reactions. Traditionally, this operation mode is implemented by periodically shifting inlet and outlet sections so as to jump a single reactor unit in the flow direction. Here, a network of four catalytic reactors carrying on the methanol synthesis process is considered and the effect of varying the number (n s) of reactor units jumped by inlet and outlet sections on network stability and performance is investigated. Increasing n s, a greater variety of periodic regimes giving rise to trains of temperature waves characterized by spatial periodicity are detected as the switching velocity varies. These regimes well reproduce the inter-stage cooling effect of multistage fixed bed reactors and, hence, guarantee in general large conversion values. Moreover, an intriguing coexistence between T-periodic and multi-periodic temperature wave trains is revealed, T being the period needed for the system to recover its initial configuration. A T-periodic symmetric wave train characterized by k waves always coexists with a number of k-1 stable symmetric kT-periodic regimes, except when symmetry breaking is encountered. The k-1 coexisting regimes correspond to wave trains with a number of waves ranging between 1 and k-1. Bifurcational analysis is performed to characterize the stability range of periodic regimes and to systematically analyze multiplicities and bifurcations as the switching velocity is varied and at different n s. © 2011 Elsevier B.V.
2011
bifurcation analysis; loop reactor; multistability; pattern formation; periodically forced network; process intensification; waves train
01 Pubblicazione su rivista::01a Articolo in rivista
Multiplicities of temperature wave trains in periodically forced networks of catalytic reactors for reversible exothermic reactions / Erasmo, Mancusi; Altimari, Pietro; Lucia, Russo; Crescitelli, Silvestro. - In: CHEMICAL ENGINEERING JOURNAL. - ISSN 1385-8947. - STAMPA. - 171:2(2011), pp. 655-668. [10.1016/j.cej.2011.04.026]
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Utilizza questo identificativo per citare o creare un link a questo documento: https://hdl.handle.net/11573/476474
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