Revisiting the effect of U-bends, flow parameters, and feasibility for scale-up on residence time distribution curves for a continuous bioprocessing oscillatory baffled flow reactor
dc.contributor.author | Cox, Rylan | |
dc.contributor.author | Salonitis, Konstantinos | |
dc.contributor.author | Rebrov, Evgeny | |
dc.contributor.author | Impey, Susan A. | |
dc.date.accessioned | 2022-07-25T15:48:39Z | |
dc.date.available | 2022-07-25T15:48:39Z | |
dc.date.issued | 2022-07-18 | |
dc.description.abstract | Abstract An oscillatory baffled flow reactor (OBR) has been designed with 60 interbaffled cells. The baffled columns of 40 mm internal diameter together result in a reactor length of 5740 mm. The oscillatory amplitude and frequency were in the range of 2–12 mm and 0.3–2 Hz, respectively. The report investigates the impact of U-bends and the number of reactor sections on axial dispersion for scale-up feasibility. A prediction model using operating parameters has been developed to maximize plug flow conditions using the tanks-in-series (TiS) model. The maximum TiS value was 13.38 in a single column compared to 43.68 in the full reactor at a velocity ratio of 2.27 using oscillatory parameters 8 mm and 0.3 Hz. The mixing efficiency along the reactor was found to decrease after each column at amplitudes <6 mm compared to amplitudes up to 12 mm, where a negligible impact was observed. U-bend geometry had a significant role in the decrease of TiS values. | en_UK |
dc.identifier.citation | Cox R, Salonitis K, Rebrov E, Impey SA. (2022) Revisiting the effect of U-bends, flow parameters, and feasibility for scale-up on residence time distribution curves for a continuous bioprocessing oscillatory baffled flow reactor. Industrial and Engineering Chemistry Research, Volume 61, Issue 30, 3 August 2022, pp. 11181–11196 | en_UK |
dc.identifier.issn | 0888-5885 | |
dc.identifier.uri | https://doi.org/10.1021/acs.iecr.2c00822 | |
dc.identifier.uri | https://dspace.lib.cranfield.ac.uk/handle/1826/18228 | |
dc.language.iso | en | en_UK |
dc.publisher | American Chemical Society | en_UK |
dc.rights | Attribution 4.0 International | * |
dc.rights.uri | http://creativecommons.org/licenses/by/4.0/ | * |
dc.subject | Oscillatory Baffled Flow Reactor | en_UK |
dc.subject | Tanks-in-Series | en_UK |
dc.subject | Velocity Ratio | en_UK |
dc.subject | Scale-Up Feasibility | en_UK |
dc.subject | U-Bends | en_UK |
dc.title | Revisiting the effect of U-bends, flow parameters, and feasibility for scale-up on residence time distribution curves for a continuous bioprocessing oscillatory baffled flow reactor | en_UK |
dc.type | Article | en_UK |
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