Influence of Membrane Type on Some Electrical Properties of a Single Microbial Fuel Cell
H. Bouzidi, L. Otmani, R. Doufnoune, L. Zerroual +1
AI summary
72% confidenceThis paper investigates two custom proton exchange membranes (PVA/PSSNa and PVC-MTOA) in single-chamber air-cathode microbial fuel cells using wastewater and synthetic medium. PVA/PSSNa achieved higher power density (18.24 mW/cm²) and lower internal resistance (54 Ω) compared to PVC-MTOA (9.64 mW/cm², 350 Ω), attributed to superior proton conductivity and membrane stability. The study characterizes membrane properties via FTIR, SEM, DSC, TGA, and contact angle, then correlates these to electrochemical performance over five weeks of operation.
Key insights
Performance PVA/PSSNa membrane delivered 1.89× higher maximum power density (18.24 vs 9.64 mW/cm²) and 6.5× lower internal resistance (54 vs 350 Ω) than PVC-MTOA, driven by ionic conductivity difference of 12.2× (1.02×10⁻⁴ vs 8.37×10⁻⁶ S/cm).
So what. Prioritize sulfonic acid-bearing membranes (PVA/PSSNa type) over ionic liquid-based designs (PVC-MTOA) when proton transport and sustained power output are critical; the 78% vs 86% swelling rates show PVC-MTOA absorbs more water but conducts protons poorly.
Trade-off PVA/PSSNa power output declined 73% over five weeks (18.24 → 4.98 mW/cm²), while PVC-MTOA showed non-monotonic behavior, peaking at week 4 (9.64 mW/cm²) before dropping to 5.26 mW/cm² by week 5.
So what. Expect membrane aging and biofilm restructuring to degrade performance; PVA/PSSNa degrades steadily while PVC-MTOA exhibits transient recovery, suggesting different fouling or microbial colonization kinetics—monitor both membranes weekly and plan for maintenance or replacement cycles.
Threshold Internal resistance of PVC-MTOA increased 3.4× after discharge (350 → 1200 Ω) versus negligible change in PVA/PSSNa (54 → 62 Ω), indicating membrane-specific aging mechanisms.
So what. PVC-MTOA membranes are prone to rapid degradation under discharge; if long-term operation is required, PVA/PSSNa is more durable, but plan for replacement of either membrane within 4–5 weeks in this configuration.
Mechanism Open circuit voltage (OCV) for PVA/PSSNa was 604 mV (week 1) versus 156 mV for PVC-MTOA (week 1), a 3.87× difference, yet both used identical electrode materials and wastewater substrate.
So what. Membrane ionic conductivity and proton transport efficiency directly set the thermodynamic potential available; use OCV as a rapid diagnostic for membrane quality before committing to long-term operation.
Opportunity areas6
Specific gaps in this paper, with an experiment that would close each.
High No nitrogen species (NO₃⁻, NO₂⁻, NH₄⁺, N₂O) were measured in the anolyte or catholyte despite use of wastewater and synthetic medium containing NH₄Cl (1.50 g/L).
Paper states 'The cathode compartment is either used to remove heavy metals or for denitrification' in introduction, yet no denitrification or nitrification data are presented; nitrogen cycling is completely absent from results.
Try. Measure NO₃⁻, NO₂⁻, NH₄⁺, and N₂O concentrations weekly in both chambers using ion chromatography or gas chromatography; correlate with cathode potential and dissolved oxygen.
High Cathode potential and anode potential were not independently controlled or reported; only external resistance (5 kΩ) and resulting voltage/current are given.
Paper states 'The anode potential should be low and the cathode potential should be high in order to have a maximum fuel cell performance' but provides no potentiostat data, making it impossible to assess whether potentials were optimized or to predict performance under different operating regimes.
Try. Operate cells with potentiostat in galvanostatic or potentiostatic mode; vary anode potential from −0.3 to +0.2 V vs Ag/AgCl and cathode potential from +0.4 to +0.8 V; measure power, current, and nitrogen species at each setpoint.
Medium Dissolved oxygen (DO) concentration in the anolyte was not monitored, yet oxygen is a competing electron acceptor that can suppress biofilm formation and denitrification.
Single-chamber design with air cathode may allow oxygen diffusion into anode; no DO measurements reported despite relevance to microbial metabolism and nitrogen cycling.
Try. Measure DO in anolyte weekly using optical probe; correlate with power output and biofilm morphology; test anaerobic vs aerobic anode conditions.
Medium Catholyte pH was not reported or controlled, yet pH strongly affects proton transport, oxygen reduction kinetics, and potential denitrification or nitrification at the cathode.
Synthetic medium composition is given but final pH is not stated; no pH adjustment or monitoring during operation is mentioned.
Try. Measure and control catholyte pH (target 6.5–8.5); vary pH in steps of 0.5 units; measure power density, OCV, and nitrogen species (if denitrification is intended).
Medium Hydraulic retention time (HRT) and substrate loading rate were not defined; medium was 'filled every week' but volume exchanged and residence time are unclear.
Paper does not specify whether the entire 200 mL was replaced weekly or partially refreshed, making it impossible to calculate organic loading rate or HRT.
Try. Define HRT explicitly (e.g., 7 days for weekly refresh); vary HRT from 3 to 14 days; measure COD removal, power output, and nitrogen species accumulation.
Medium Biofilm composition and microbial community structure were not characterized despite being central to MFC performance; only bulk electrical properties are reported.
Paper mentions 'bio-film formed' and states that 'electricity generation and stability of MFCs are radically affected by the microbial communities on the electrode surface' but provides no 16S rRNA, microscopy, or electrochemical impedance data on biofilm.
Try. Perform 16S rRNA gene sequencing on anode biofilm; use confocal microscopy to visualize biofilm thickness and structure; correlate with power output and nitrogen cycling rates.
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What they did
- System
- MFC
What worked
Abstract
The effects of different parameters on the electric output of air-cathode microbial fuel cells were investigated in this work. The single microbial fuel cell was equipped by modifying Proton Exchange Membranes (PEM). Two membrane types were prepared: first by using the combination of Poly Vinyl Alcohol (PVA) with Polystyrene Sulfonate (PSSNa), while the second membrane was elaborated by mixing Poly Vinyl Chloride (PVC) with Methyl Tri-Octyl Ammonium (MTOA) chloride. The PEMs were incorporated into the air-cathode to form a Membrane Electrode Assembly (MEA) to promote electricity generation. PVA/PSSNa and PVC-MTOA membranes were synthesized by solution casting method. Fourier Transform Infrared Spectroscopy (FTIR), Ultraviolet (UV) Visible spectroscopy, Scanning Electronique Microscope (SEM), Differential Scanning Calorimetry (DSC), and water Contact Angle (CA) were used as characterization techniques to explore the membrane structure and properties. The performance and the electric capacity of the microbial fuel cell in real time were operated using an external resistance of 5kΩ. Impedance and resistance capacity were determined using the polarization method. It was found that the internal resistance of the PVA/PSSNa and PVC-MTOA membranes were 50 and 350Ω respectively. The voltage values at open circuit of the cells using PVA/PSSNa and PVC-MTOA membranes were 600mV and 150mV respectively. The values of power, current, and power density, are quite interesting. Cells with PVA/PSSNa and PVC-MTOA membranes gave values of 18.24 and 9.64mW.cm⁻² respectively.
Keywords
Identifiers
- Journal
- Engineering, Technology & Applied Science Research
- Year
- 2022
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