Corrigendum to “Liquid backmixing in an inclined rotating tubular fixed bed reactor – Augmenting liquid residence time via flow regime adjustment” [Chem. Eng. Process. Process Intensif. (2015) 2–10] (Chemical Engineering and Processing - Process Intensification (2015) 94 (2–10), (S0255270115000392), (10.1016/j.cep.2015.02.003))
Research output: Contribution to specialist publication › Corrections (errata and retractions) › peer-review
Contributors
Abstract
The authors regret to inform that an error occurred in Eq. (2), Eq. (7) as well as Figs. 3, 6 and 7 of the article with the aforementioned title. In the equations, the mean real liquid velocity (vL) should be applied instead of the fluid superficial velocity (uL): [Formula presented] [Formula presented] The equations are related to the fitted curves based on the axial dispersion model (Fig. 3) and to the extracted axial dispersion coefficients (Figs. 6 and 7). The correct figures are now presented via this corrigendum. It is worth mentioning that none of these mistakes affects the originality of the article's text and the presented results. The authors would like to apologise for any inconvenience caused.
Details
Original language | English |
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Pages | 108087 |
Volume | 156 |
Journal | Chemical Engineering and Processing - Process Intensification |
Publication status | Published - Oct 2020 |
Peer-reviewed | Yes |