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- W2043131483 abstract "Abstract Plug flow as well as axial dispersion dynamic models for counter-flow extractive reactors are formulated and solved to investigate the frequency response characteristics of such reactors. The reactions considered are taken to be either infinitely fast, taking place at the interface between the two phases or within a thin film in one of the phases, or slow taking place in the bulk of one of the phases. The results demonstrate the effect of the kinetic regime as well as axial dispersion (Peclet number) of the continuous phase on the dynamic behaviour of the two phase reactor. For the plug flow case (P e → ∞) it is shown that for some input-output relations the kinetic regime affects the functional forms of the transfer functions. The complex transfer functions are approximated, using simple fitting techniques, to simpler ones suitable for the design of the reactor's control loops. For the axial dispersion case the results show that the continuous phase Peclet number affects the frequency response of the reactor in a complicated manner giving rise, for some input-output relations and small values of the Peclet number, to complex oscillations in both amplitude ratio and phase angle." @default.
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- W2043131483 date "1978-01-01" @default.
- W2043131483 modified "2023-09-27" @default.
- W2043131483 title "Effect of kinetic regime and axial dispersion on the dynamic response of counter flow extractive reactors" @default.
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- W2043131483 doi "https://doi.org/10.1016/0009-2509(78)85174-4" @default.
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