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Investigating the effects of fluidic connection between microbial fuel cells

Investigating the effects of fluidic connection between microbial fuel cells
Investigating the effects of fluidic connection between microbial fuel cells
Microbial fuel cells (MFCs) can ‘treat’ wastewater but individually are thermodynamically restricted. Scale-up might, therefore, require a plurality of units operating in a stack which could introduce losses simply through fluidic connections. Experiments were performed on two hydraulically joined MFCs (20 cm apart) where feedstock flowed first through the upstream unit (MFCup) and into the downstream unit (MFCdown) to explore the interactive effect of electrical load connection, influent make-up and flow-rate on electrical outputs. This set-up was also used to investigate how calculating total internal resistance based on a dynamic open circuit voltage (OCV) might differ from using the starting OCV. When fed a highly conductive feedstock (~4,800 μS) MFCdown dropped approximately 180 mV as progressively heavier loads were applied to MFCup (independent of flow-rate) due to electron leakages through the medium. The conductivities of plain acetate solutions (5 and 20 mM) were insufficient to induce losses in MFCdown even when MFCup was operating at high current densities. However, at the highest flow-rate (240 mL/h) MFCdown dropped by approximately 100 mV when using 5 and 220 mV using 20 mM acetate. When the distance between MFCs was reduced by 5 cm, voltage drops were apparent even at lower flow-rates, (30 mL/h decreased the voltage by 115 mV when using 20 mM acetate). Shear flow-rates can introduce dissolved oxygen and turbulence all capable of affecting the anodic biofilm and redox conditions. Calculating total internal resistance using a dynamic OCV produced a more stable curve over time compared to that based on the starting constant OCV.
Microbial fuel cell, Internal resistance, Wastewater treatment, Open circuit voltage, Stack
1615-7591
477-484
Winfield, Jonathan
e81f4fad-1433-4c6a-9723-24a14f172896
Ieropoulos, Ioannis
6c580270-3e08-430a-9f49-7fbe869daf13
Greenman, John
eb3d9b82-7cac-4442-9301-f34884ae4a16
Dennis, Julian
25bd2523-2802-498f-9a17-80ecea7db112
Winfield, Jonathan
e81f4fad-1433-4c6a-9723-24a14f172896
Ieropoulos, Ioannis
6c580270-3e08-430a-9f49-7fbe869daf13
Greenman, John
eb3d9b82-7cac-4442-9301-f34884ae4a16
Dennis, Julian
25bd2523-2802-498f-9a17-80ecea7db112

Winfield, Jonathan, Ieropoulos, Ioannis, Greenman, John and Dennis, Julian (2011) Investigating the effects of fluidic connection between microbial fuel cells. Bioprocess and Biosystems Engineering, 34 (4), 477-484. (doi:10.1007/s00449-010-0491-x).

Record type: Article

Abstract

Microbial fuel cells (MFCs) can ‘treat’ wastewater but individually are thermodynamically restricted. Scale-up might, therefore, require a plurality of units operating in a stack which could introduce losses simply through fluidic connections. Experiments were performed on two hydraulically joined MFCs (20 cm apart) where feedstock flowed first through the upstream unit (MFCup) and into the downstream unit (MFCdown) to explore the interactive effect of electrical load connection, influent make-up and flow-rate on electrical outputs. This set-up was also used to investigate how calculating total internal resistance based on a dynamic open circuit voltage (OCV) might differ from using the starting OCV. When fed a highly conductive feedstock (~4,800 μS) MFCdown dropped approximately 180 mV as progressively heavier loads were applied to MFCup (independent of flow-rate) due to electron leakages through the medium. The conductivities of plain acetate solutions (5 and 20 mM) were insufficient to induce losses in MFCdown even when MFCup was operating at high current densities. However, at the highest flow-rate (240 mL/h) MFCdown dropped by approximately 100 mV when using 5 and 220 mV using 20 mM acetate. When the distance between MFCs was reduced by 5 cm, voltage drops were apparent even at lower flow-rates, (30 mL/h decreased the voltage by 115 mV when using 20 mM acetate). Shear flow-rates can introduce dissolved oxygen and turbulence all capable of affecting the anodic biofilm and redox conditions. Calculating total internal resistance using a dynamic OCV produced a more stable curve over time compared to that based on the starting constant OCV.

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More information

Accepted/In Press date: 17 November 2010
e-pub ahead of print date: 7 December 2010
Published date: May 2011
Keywords: Microbial fuel cell, Internal resistance, Wastewater treatment, Open circuit voltage, Stack

Identifiers

Local EPrints ID: 454658
URI: http://eprints.soton.ac.uk/id/eprint/454658
ISSN: 1615-7591
PURE UUID: cf194466-87fa-421d-85cc-420d655bb238
ORCID for Ioannis Ieropoulos: ORCID iD orcid.org/0000-0002-9641-5504

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Date deposited: 18 Feb 2022 17:34
Last modified: 17 Mar 2024 04:10

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Contributors

Author: Jonathan Winfield
Author: John Greenman
Author: Julian Dennis

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