Salvato in:
Dettagli Bibliografici
Autore principale: Aschmoneit, Fynn Jerome
Natura: Preprint
Pubblicazione: 2025
Soggetti:
Accesso online:https://arxiv.org/abs/2502.07091
Tags: Aggiungi Tag
Nessun Tag, puoi essere il primo ad aggiungerne!!
_version_ 1866910822014386176
author Aschmoneit, Fynn Jerome
author_facet Aschmoneit, Fynn Jerome
contents This study presents a detailed quantification of how flow orientation affects mass transfer and frictional resistance in periodically confined channels, offering novel insights into the physical similarity relations governing these phenomena. We constitute that the Sherwood number and friction factor adhere to universal scaling laws of the form $ Sh = A \Bigl( 1 + B \, \sin(2α) \Bigr) Re^\frac{1}{2}$ and $ f = A \Bigl( 1 + B \, \sin(2α) \Bigr) Re^{-\frac{1}{2}}$, where $α$ depicts the orientation of the periodically confined channel. It is found that the flow orientation and the cross flow velocity independently affect both, the Sherwood number and the friction factor. A key contribution of this work is the explicit characterization of the flow orientation: a 45° rotation of the flow relative to the spacer structure increases the Sherwood number by nearly 25\%, while the friction factor rises by approximately 20\%. These findings highlight a fundamental trade-off between mass transfer enhancement and flow resistance, suggesting that any process optimization must carefully balance the gains in mixing efficiency against the increased energy dissipation. This study provides a robust framework for further investigations into how periodic geometrical constraints influence transport processes in complex flow systems.
format Preprint
id arxiv_https___arxiv_org_abs_2502_07091
institution arXiv
publishDate 2025
record_format arxiv
spellingShingle Mass Transfer and Pressure Drop Similarities in Oriented, Periodically Confined Channels
Aschmoneit, Fynn Jerome
Fluid Dynamics
This study presents a detailed quantification of how flow orientation affects mass transfer and frictional resistance in periodically confined channels, offering novel insights into the physical similarity relations governing these phenomena. We constitute that the Sherwood number and friction factor adhere to universal scaling laws of the form $ Sh = A \Bigl( 1 + B \, \sin(2α) \Bigr) Re^\frac{1}{2}$ and $ f = A \Bigl( 1 + B \, \sin(2α) \Bigr) Re^{-\frac{1}{2}}$, where $α$ depicts the orientation of the periodically confined channel. It is found that the flow orientation and the cross flow velocity independently affect both, the Sherwood number and the friction factor. A key contribution of this work is the explicit characterization of the flow orientation: a 45° rotation of the flow relative to the spacer structure increases the Sherwood number by nearly 25\%, while the friction factor rises by approximately 20\%. These findings highlight a fundamental trade-off between mass transfer enhancement and flow resistance, suggesting that any process optimization must carefully balance the gains in mixing efficiency against the increased energy dissipation. This study provides a robust framework for further investigations into how periodic geometrical constraints influence transport processes in complex flow systems.
title Mass Transfer and Pressure Drop Similarities in Oriented, Periodically Confined Channels
topic Fluid Dynamics
url https://arxiv.org/abs/2502.07091