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Simulation of a vanadium-cerium redox flow battery incorporating graphite felt electrodes

Simulation of a vanadium-cerium redox flow battery incorporating graphite felt electrodes
Simulation of a vanadium-cerium redox flow battery incorporating graphite felt electrodes

Computational fluid dynamics (CFD) simulations are used to predict the electrolyte dispersion, mass transport, current–potential distributions and state of charge in a vanadium-cerium redox flow battery (RFB) containing graphite felt electrodes, the half-cell flow compartments being separated by an anion exchange membrane. A polymeric mesh was placed between graphite felt and membrane; the anolyte and catholyte were pumped to separate stirred tanks in the batch recirculation mode. The simulation of single-phase flow was performed using the Brinkman and Navier-Stokes equations to describe flow dispersion within the graphite felt and polymeric mesh, respectively. At the same time, mass transport and current distribution were computed by solving mass and charge conservation equations. Fluid dynamics revealed a periodic velocity distribution within the porous electrode, which was influenced by the polymer mesh between electrode and membrane. A mean fractional conversion of 0.005 per pass was achieved. During a galvanostatic cycle, the state of charge fell from 36 to 10% over a 70 min discharge then rose from 10 to 30% during charge. A relatively uniform potential distribution was achieved along the length of the graphite felt in the presence of the low conversion per pass. The numerical model demonstrated a good agreement between the predicted and experimental cell potential and state of charge, with an average deviation below 0.12%. The unit cell RFB performance showed voltage, coulombic, and energy efficiencies of 85, 83, and 70%, respectively. A numerical model of the vanadium-cerium RFB served as the first approach to a more robust experimental study.

CFD simulations, Current distribution, Mass transport, Porous electrodes, Redox flow battery (RFB), State of charge (SOC)
1572-6657
León, María I.
417a500e-6f82-4847-ad70-08245dcadb0c
Arenas, Luis F.
6e7e3d10-2aab-4fc3-a6d4-63a6614d0403
Walsh, Frank C.
309528e7-062e-439b-af40-9309bc91efb2
Nava, José L.
fbc212cd-8011-4642-8c1f-300b524061f8
León, María I.
417a500e-6f82-4847-ad70-08245dcadb0c
Arenas, Luis F.
6e7e3d10-2aab-4fc3-a6d4-63a6614d0403
Walsh, Frank C.
309528e7-062e-439b-af40-9309bc91efb2
Nava, José L.
fbc212cd-8011-4642-8c1f-300b524061f8

León, María I., Arenas, Luis F., Walsh, Frank C. and Nava, José L. (2021) Simulation of a vanadium-cerium redox flow battery incorporating graphite felt electrodes. Journal of Electroanalytical Chemistry, 903, [115847]. (doi:10.1016/j.jelechem.2021.115847).

Record type: Article

Abstract

Computational fluid dynamics (CFD) simulations are used to predict the electrolyte dispersion, mass transport, current–potential distributions and state of charge in a vanadium-cerium redox flow battery (RFB) containing graphite felt electrodes, the half-cell flow compartments being separated by an anion exchange membrane. A polymeric mesh was placed between graphite felt and membrane; the anolyte and catholyte were pumped to separate stirred tanks in the batch recirculation mode. The simulation of single-phase flow was performed using the Brinkman and Navier-Stokes equations to describe flow dispersion within the graphite felt and polymeric mesh, respectively. At the same time, mass transport and current distribution were computed by solving mass and charge conservation equations. Fluid dynamics revealed a periodic velocity distribution within the porous electrode, which was influenced by the polymer mesh between electrode and membrane. A mean fractional conversion of 0.005 per pass was achieved. During a galvanostatic cycle, the state of charge fell from 36 to 10% over a 70 min discharge then rose from 10 to 30% during charge. A relatively uniform potential distribution was achieved along the length of the graphite felt in the presence of the low conversion per pass. The numerical model demonstrated a good agreement between the predicted and experimental cell potential and state of charge, with an average deviation below 0.12%. The unit cell RFB performance showed voltage, coulombic, and energy efficiencies of 85, 83, and 70%, respectively. A numerical model of the vanadium-cerium RFB served as the first approach to a more robust experimental study.

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More information

Accepted/In Press date: 2 November 2021
e-pub ahead of print date: 8 November 2021
Published date: 15 November 2021
Additional Information: Publisher Copyright: © 2021 Elsevier B.V.
Keywords: CFD simulations, Current distribution, Mass transport, Porous electrodes, Redox flow battery (RFB), State of charge (SOC)

Identifiers

Local EPrints ID: 500766
URI: http://eprints.soton.ac.uk/id/eprint/500766
ISSN: 1572-6657
PURE UUID: 5ffbb592-d383-41ec-890e-23df8c6269db
ORCID for Luis F. Arenas: ORCID iD orcid.org/0000-0002-9579-5082

Catalogue record

Date deposited: 13 May 2025 16:34
Last modified: 14 May 2025 01:55

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Contributors

Author: María I. León
Author: Luis F. Arenas ORCID iD
Author: Frank C. Walsh
Author: José L. Nava

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