Ankita
Chaurasiya†
ab,
Yashmeen
Budania†
ab,
Goldy
Shah
c,
Aradhana
Mishra
bd and
Shiv
Singh
*ab
aIndustrial Waste Utilization, Nano and Biomaterials, Council of Scientific and Industrial Research – Advanced Materials and Processes Research Institute, Bhopal, 462026, India. E-mail: sshiv.ampri@csir.res.in; sshiviitk@gmail.com
bAcademy of Scientific and Innovative Research, Ghaziabad, 201002, Uttar Pradesh, India
cIndian Institute of Technology Delhi, New Delhi 110016, India
dDivision of Microbial Technology, CSIR – National Botanical Research Institute, Lucknow, 226001, Uttar Pradesh, India
First published on 20th June 2025
The growing demand for sustainable energy and effective wastewater treatment has propelled the advancement of bio-electrochemical systems (BESs), particularly microbial fuel cells (MFCs) and microbial electrolysis cells (MECs). These systems integrate bioelectricity generation with organic and inorganic pollutant degradation, offering a sustainable solution for environmental remediation. However, challenges such as high overpotential, reliance on noble metal electrodes, and inconsistent performance have necessitated innovative improvements. The incorporation of photocatalysis into BESs has led to the development of photo-bio-electrochemical systems (PBESs), including photo-microbial fuel cells (PMFCs) and photo-microbial electrolysis cells (PMECs), which leverage optical energy to enhance efficiency. Carbon-based electrode materials, owing to their high porosity, conductivity, and biocompatibility, have emerged as ideal candidates for improving PBES performance. Advanced carbon nanostructures, such as graphene, carbon nanotubes, and metal-graphitic carbon nitride composites, have demonstrated superior photocatalytic properties, promoting enhanced charge separation, CO2 reduction, hydrogen production, and wastewater treatment. PBES integrating light-activated semiconductor materials with BESs, further amplify pollutant degradation and energy conversion efficiency. Despite significant progress, optimizing electrode materials and improving charge transport remain key challenges for scalable and cost-effective deployment. This review highlights the latest advancements in carbon-based electrodes for PBESs, detailing their mechanisms, photocatalytic properties, and future prospects in sustainable energy production and environmental remediation. By addressing existing material limitations and exploring novel photocatalytic enhancements, this work aims to contribute to the development of next-generation PBESs, fostering circular economy practices and carbon-neutral energy solutions.
Wider impactPhoto-bio-electrochemical systems (PBESs), including photo-microbial fuel cells (PMFCs) and photo-microbial electrolysis cells (PMECs), offer sustainable solutions to global challenges of energy scarcity, environmental pollution, and wastewater management. By integrating photocatalysis with renewable energy generation and wastewater treatment, PBESs contribute to circular economy principles, enabling resource recovery while reducing carbon emissions. These systems uniquely combine solar energy utilization with microbial electrochemical processes to produce green electricity, hydrogen, and clean water, positioning them as transformative technologies for sustainable urban development and environmental remediation. Photocatalysis plays a pivotal role in enhancing the efficiency of PBESs by harnessing solar energy for improved degradation of recalcitrant pollutants and enhanced electron transfer processes. Carbon-based electrodes, known for their excellent conductivity, affordability, and environmental compatibility, are particularly effective in boosting photocatalytic performance. They enhance power output, improve coulombic efficiency, and support the degradation of complex compounds in wastewater, thereby optimizing the efficiency and scalability of microbial fuel cells (MFCs) and microbial electrolysis cells (MECs). Despite these advantages, challenges such as high overpotentials, membrane biofouling, oxygen diffusivity, and instability of electrode materials hinder the large-scale application of PBESs. Addressing these challenges requires continued research in advanced photocatalytic materials, innovative catalytic systems, and cost-effective membrane technologies. Interdisciplinary collaboration among material scientists, environmental engineers, and energy specialists is crucial to overcoming these limitations. Furthermore, strategic investments and supportive policies are needed to accelerate the commercialization of PBESs. Integrating these systems into industrial and municipal wastewater treatment facilities can revolutionize sustainable urban infrastructure by enabling energy-positive water treatment plants. Additionally, their application in decentralized energy systems and remote environmental monitoring presents new opportunities for off-grid energy solutions, especially in resource-constrained regions. As the world transitions towards renewable energy systems, PBESs hold significant potential to contribute to global sustainability goals by bridging the gap between environmental management, renewable energy generation, and photocatalysis. By maximizing resource recovery, enhancing pollutant degradation, and minimizing environmental impact, these technologies are poised to play a pivotal role in achieving a circular economy and ensuring a sustainable and resilient energy future. |
In addition, MECs have emerged as an advanced BES variant with the ability to convert carbon dioxide (CO2), a major greenhouse gas and primary byproduct of fossil fuel combustion, into high-value biofuels and chemicals. Through microbial metabolism and external electrical input, MECs efficiently produce hydrogen, formate, acetate, methane, butyrate, and various alcohols, offering a low-energy, carbon-neutral pathway for biofuel synthesis. This capability positions MECs as a viable solution for carbon capture, resource recovery, and sustainable bioenergy generation.17–22
To further enhance the performance of BESs, advanced oxidation processes (AOPs) have been incorporated into these systems. AOPs are known for their ability to decompose a wide range of organic pollutants by generating highly reactive species such as hydroxyl radicals (˙OH), holes (h+), and other reactive oxygen species (ROS). The integration of AOPs into BESs enhances pollutant degradation, accelerates organic matter breakdown, and improves overall system efficiency. This hybrid approach not only maximizes wastewater purification but also optimizes energy recovery, making it a promising strategy for next-generation bioelectrochemical technologies.1,23,24 With continued advancements in materials science, electrode engineering, and system optimization, BESs hold immense potential for addressing pressing global challenges related to wastewater management, renewable energy production, and carbon mitigation. Future research should focus on improving scalability, cost-effectiveness, and operational efficiency to facilitate real-world applications of these sustainable technologies. The integration of BESs with complementary strategies such as photocatalysis and AOPs further strengthens their role as a key enabler of green energy and environmental sustainability.6
The shift toward sustainable, environmentally friendly, and cost-effective electricity generation has become a global priority. According to the International Energy Agency, the reliance on fossil fuels for electricity production has been declining since 2019, coinciding with the increasing adoption of renewable energy sources.25 Projections indicate that solar photovoltaic technology will become the dominant electricity source before 2040, and by 2050, renewable sources are expected to account for 70% of global electricity generation. Among these, green hydrogen has emerged as a key energy carrier due to its environmentally benign nature. Produced through electrolysis powered by renewable energy sources such as solar, wind, and hydroelectric power, green hydrogen offers a sustainable alternative that emits no greenhouse gases during its production or use.26 In pursuit of this objective, MECs have been explored as a promising technology for biohydrogen production. A hybrid system integrating an MFC with a bio-photo-electrochemical cell (BPEC), where the BPEC photocathode is illuminated with visible light and the MFC supplies the electrolysis voltage, has been demonstrated for efficient hydrogen generation.27 Furthermore, MECs have shown remarkable potential for CO2 reduction, utilizing photo-electrodes as either the anode, cathode, or both, to drive conversion processes.28 Another variation, the photo-MECs (PMECs), leverages the synergistic interaction between a semiconductor-based photocathode and a bio-anode to simultaneously extract energy from organic pollutants and sunlight.29 Compared to photosynthesis and dark fermentation, MECs offer superior hydrogen production efficiency due to their higher yield and lower energy input.27 A critical aspect in advancing MEC technology lies in the development of efficient electrode materials for CO2 reduction and hydrogen evolution. As a central component, the cathode must exhibit high biocompatibility, surface area, conductivity, and cost-effectiveness.18,30 Carbon-based materials meet these criteria, offering diverse structural variations such as traditional carbon materials (activated carbon (AC), carbon cloth, graphite, carbon brush), nanocarbon materials (graphene, carbon nanotubes (CNT)), and metal carbide–carbon composites, many of which exhibit photo-electrochemical properties essential for MEC applications. While metal-based catalysts typically enhance hydrogen evolution rates, their high cost and potential environmental impact due to metal dissolution have limited their widespread adoption in MECs.18,27
Despite significant progress, there remains a need for a comprehensive review focusing specifically on carbon-based photocatalytic materials for BES. This review aims to provide researchers with an in-depth analysis of the role of carbon-based electrodes in CO2 reduction and hydrogen production under visible and ultraviolet irradiation along with bioenergy generation. By outlining the fundamental principles, reaction mechanisms, and relevant chemical equations, this review seeks to serve as a foundation for advancing research in this field. As the world transitions toward carbon-neutral energy sources and embraces the principles of a circular economy, BESs have emerged as a promising solution. A long series of fabrication methods of electrodes is also reported for BESs, as shown in Table 1, highlighting the advantages and drawbacks of the respective methods.
| System | Electrode | Fabrication method | Pros | Cons | Ref. |
|---|---|---|---|---|---|
| Where CF represents carbon felt, GO is graphene oxide, rGO is reduced GO, ACF is activated carbon fiber, and CNF is carbon nanofiber. | |||||
| MFC | Waste-extracted biochar | Thermochemical activation | Economical, simple and highly effective in enriching the physiochemical properties | Need of high temperature and chemicals (NaOH, KOH) | 31 |
| MFC | Graphene/TiO2/CF | Spray coating | Simple, fast and efficient to obtain a uniform distribution | Proper surface preparation and high temperature is needed | 32 and 33 |
| MEC | 3D-Synthetic biofilm/carbon cloth | 3D-bioprinting | Increase the surface area for the growth of biofilms and enhance the efficiency of MES | It is challenging to utilize the conventional technique to precisely fabricate the electrode with geometrical complexity | 34 and 35 |
| MEC | MXene-coated CF | Dip coating | Low cost and simple adjustment of layer thickness | Slow process, high risk of uneven coating | 34 and 36 |
| MEC | Mn/CF | Electrodeposition | Develops a uniform and pristine film without any contamination of other elements | Need of expensive equipment and is a time-consuming process | 37 |
| MEC | rGO-TEPA/carbon cloth | Self-assembly method | Simultaneous reduction of GO to rGO and formation of rGO-biofilm hybrid electrode | Only individual graphene-based electrodes can be fabricated | 38 |
| MFC | Ni-ACF/CNF | Chemical vapour deposition | Highly conformal and high-purity coating can be performed | Slow deposition rate, expensive equipment and high temperature needed | 4 |
| MFC | Au/carbon paper composite | Sputtering | Deposit thin, uniform, smooth and durable films. | Requires expensive vacuum systems. | 39 |
However, their widespread implementation is hindered by challenges related to material cost, durability, and stability. Carbon-based materials are recognised as cost-effective, abundant, durable and biocompatible compared to other classes of materials (metal, metal–oxide, conductive polymer, ceramic, and covalent organic frameworks (COFs) or metal organic frameworks (MOFs)-based) as shown in a summary table illustrating the advantages and limitations of various types of materials in BESs (Table 2). To address these limitations, research is increasingly focused on developing carbon-based electrocatalysts that are abundant, cost-effective, and exhibit inherent photocatalytic properties. This review highlights innovations in electrode materials aimed at enhancing the sustainability and performance of photo-enhanced MFCs and MECs. Reflecting this concern, Fig. 1 illustrates advancements in carbon-based electrodes for photo-MFCs (PMFCs) and PMECs over the past five years.
| Electrode material | Advantages | Limitation | Ref. |
|---|---|---|---|
| Where EET is the abbreviation for extracellular electron transfer. | |||
| Graphene-based | 2D-carbon materials provide a larger surface area for bacterial attachment and extracellular electron transfer | High cost and mass production are challenging | 40 |
| CNT | 1D material amplifies EET processes more than bare glassy carbon electrodes | Less efficient for EET processes than 2D material | 41 |
| Carbon cloth | Highly porous and biocompatible | Low catalytic activity, requires modifications for improved performance | 42 |
| Biochar | Cost-effective and easily available | Physical or chemical treatments are needed to activate it to use it as an electrode material | 31 |
| Metal-based | Improves power generation and electron transfer kinetics | Dissolution, corrosion and some have antimicrobial properties | 43 |
| Metal oxide-based | Boost both conductivity and mechanical strength | Dissolution, metal particle agglomeration and corrosion in electrolyte solutions | 44 |
| Heteroatom doped-metal oxide/CNF/ACF | Heteroatoms are favorable to the EET between the anode and cytochrome-c on the outer membranes of bacterial cells | In some cases efficiency of post-doping is low and diverse while in the case of direct doping the pore size and porosity of the catalyst are difficult to be precisely controlled | 8 |
| Ceramic-based (fluorine doped TiO2 ceramic) | The algae-based PMFCs with the ceramic anodes are attested to be 16 times more powerful than the best performing carbon-based electrode | Power curves displayed the overshoot phenomenon, which points to a system underperformance | 45 |
| Conducting polymer-based (PEDOT:PSS-modified anode) | Improves conductivity and bacterial adhesion due to synergy between constituents | The enrichment of specific microbial cultures for industrial-scale plants is technically challenging | 46 |
| MOFs/COFs-based (PANI@COF-CNT) | High surface area and tunable porosity, enhance EETs and provide more sites for microbial activity | Expensive and complex synthesis process, sometimes its application is narrowed in BESs due to low conductivity and stability | 47 |
As research in catalyst innovations and development continues to progress, there is a growing interest in translating laboratory-scale breakthroughs into industrial-scale implementations. Despite rapid advancements in photo-electrocatalysis in recent years, its large-scale application remains underdeveloped, facing numerous critical challenges. At the laboratory scale, catalyst synthesis benefits from precise control over reaction conditions, solvent systems, stoichiometric ratios, and other parameters often resulting in high-performance materials with excellent photo-electrocatalytic activity. However, the transition to industrial-scale production reveals significant obstacles. The key issue lies in the dependence of photo-electrocatalytic properties on the exposure of active sites, which requires precise regulation of morphology, crystal formation, compositional order, and defect concentration parameters that are difficult to control on a larger scale. Although effective, techniques like atomic layer deposition, magnetron sputtering, and galvanic replacement are costly and yield limited quantities of catalyst materials. Furthermore, these techniques often lack universality and are optimized for specific catalyst types. Another critical challenge is the high cost of raw materials. Many high-performance catalysts rely on precious metals such as Pt, Pd, and Ru, or rare earth elements like La and Ce, which are expensive and limit the feasibility of large-scale production. Therefore, the development of more economical and sustainable alternatives is essential. Catalyst stability also plays a crucial role in determining suitability for scale-up. Enhancing the lifetime of catalysts reduces the replacement frequency, thereby improving productivity and cost-efficiency.48 This article highlights the potential of low-cost catalyst materials and synthesis methods for industrial-level photo-electrocatalysis. It also presents the current challenges and future directions for scalable, cost-effective, and sustainable catalyst technologies. This review provides a comprehensive overview of the theoretical foundations and practical applications of photocatalysis and AOPs, with a focus on PBESs, including PMFCs and PMECs. It begins by outlining the fundamentals of photocatalysis, incorporating both natural and artificial photosynthesis, and then explores the underlying mechanisms involved in wastewater treatment, CO2 reduction, and H2 generation. The manuscript further discusses the significance and recent developments of carbon-based electrode materials in photoelectrocatalytic processes, again emphasizing their roles in wastewater treatment, CO2 reduction, and H2 generation, and expanding into emerging trends and applications. The final section addresses research challenges, future opportunities, and key perspectives within the intersection of PBESs and carbon materials. While previous studies have reviewed electrode materials in electrochemical processes related to wastewater treatment or, more rarely, CO2 reduction and H2 generation, their focus tends to be broader covering general electrode roles, nanostructured materials for AOPs, anodic materials for electrochemical oxidation, or general developments in electrode technology.49 This review uniquely explores the potential of carbon-based materials as feasible and promising photocatalysts in PBESs, a topic that remains underexplored in current literature. The novelty of the review lies in its interdisciplinary approach and focus on integrating PMFCs and PMECs, specifically targeting environmental applications such as wastewater treatment, CO2 reduction, and hydrogen generation. This review sets itself apart by centering on recent advancements in electrode materials and their novel applications across the key areas of photocatalysis, MFCs, and MECs. The insights presented here aim to guide researchers in both experimental and industrial contexts, paving the way for scalable innovations in photocatalytic fuel systems.
| h+ + OH− → ˙OH |
| O2 + e− → ˙OH2− |
| 2O2− + 2H+ → H2O2 + O2 |
| H2O2 + e− → ˙OH + OH− |
Photocatalysis often requires an external bias to enhance performance, as the recombination of photogenerated e−/h+ pairs due to electrostatic attraction significantly reduces quantum efficiency. This necessity a bias voltage that aligns well with the bioelectricity generated by MFCs, enabling a synergistic integration of both systems. A model of bioelectricity generation in PMFCs is shown in Fig. 3. In photocatalytic fuel cells (PFCs), ROS facilitate the degradation of organic matter at the photoanode while the generated electrons are transferred to the cathode, contributing to electricity generation. This dual-functionality of simultaneous pollutant degradation and energy conversion renders PFCs a promising solution for wastewater treatment. Recent advancements have demonstrated the feasibility of PFCs in efficiently eliminating both persistent and emerging organic contaminants, making them a revolutionary technology for sustainable wastewater management.23,54,55 Photocatalysts, materials capable of absorbing photons and generating excited states, play a crucial role in photocatalytic systems. These materials exhibit desirable properties such as high optical transmittance, mechanical durability, thermal stability, and hydrophobicity, making them suitable for applications in photovoltaics, supercapacitors, electrochemical water splitting, gas sensors, and self-cleaning surfaces. Over the past decade, significant progress has been made in developing nanostructured photocatalysts with enhanced light absorption, charge separation, and catalytic efficiency. Novel inorganic, molecular, and hybrid organic–inorganic materials have been engineered to optimize oxygen evolution and facilitate efficient water splitting for hydrogen production.56 To assess the true efficiency of photocatalytic devices, it is imperative to evaluate their performance without the aid of sacrificial agents, which are often costly and impractical for large-scale applications. Instead, utilizing abundant natural resources such as seawater could provide a sustainable approach for real-world deployment. Despite the rapid expansion of photovoltaic technologies, large-scale solar-driven water-splitting modules remain an ongoing research challenge.57,58 Environmental pollution and energy shortages are two of the most pressing issues in modern society, driving the development of high-performance, eco-friendly photocatalysts for air and water purification. Semiconductor-based photocatalysis has gained significant attention due to its broad applications in energy and environmental remediation, including water splitting, CO2 reduction, and organic pollutant degradation.59 The degradation of organic contaminants via semiconductor photocatalysis involves the generation of photogenerated charge carriers, their migration to the catalyst surface, and subsequent redox reactions with adsorbed pollutants. Developing novel photocatalysts with high visible-light absorption (∼48% of sunlight) and superior photodegradation capabilities remains a key research focus, offering a sustainable pathway for addressing global environmental and energy challenges.60 The development of visible-light-sensitive photocatalysts for efficient utilization of abundant solar and indoor light has emerged as a crucial research direction in the field of photocatalysis. Extensive studies have been conducted to enhance the photocatalytic activity of materials under visible-light irradiation. Efforts have primarily focused on oxides and composite oxides, including TiO2, N-doped TiO2, Ag–TiO2, MnO2, Nb2O5, and Fe3O4/Fe2O3, as well as sulfides and composite sulfides such as CdS, ZnS, MoS2/MoS3, and Cu2ZnSnS4. These materials have demonstrated promising potential in improving light absorption and facilitating photocatalytic reactions for various environmental and energy applications.61 The Kubelka–Munk model establishes a relationship between the absorption coefficient (α) and the bandgap energy, allowing for the determination of the semiconductor's bandgap using the Tauc equation:
| (αhv)m = A(hv − Eg) |
| EVB = X − Ee + 0.5Eg |
| ECB = EVB − Eg |
First and foremost, selecting renewable and environmentally benign raw materials is essential to reduce the dependence on fossil-derived resources and promoting a more sustainable production paradigm. In parallel, minimising the use of hazardous substances and prioritising non-toxic or low-toxicity alternatives in catalyst synthesis significantly mitigates environmental and health-related concerns. Second, it is crucial to design synthesis pathways that emphasize atom economy, reduce waste generation, and streamline material and energy usage. Third, adopting efficient waste treatment and disposal strategies, alongside recycling and reusing by-products, contributes to pollution reduction and resource conservation. Fourth, integrating energy-efficient processes, particularly those powered by renewable energy sources, into catalyst production can substantially decrease greenhouse gas emissions and overall energy consumption. Among all these considerations, the activity and selectivity of photo-electrocatalysts remain paramount, as they directly influence the efficiency and viability of various catalytic reactions. Addressing these sustainability challenges can be effectively achieved by using carbon-based photo-electrocatalysts. These materials represent a promising class of catalysts due to their tunable surface chemistry, structural stability, cost-effectiveness, and high electrochemical activity. Additionally, carbon-based materials are highly modifiable, experimentally versatile, and possess excellent durability, making them ideal candidates for applications in waste treatment and renewable energy generation. Their inherent properties not only support current performance demands but also offer substantial potential for further optimization and innovation.48
Carbon-based nanomaterials, including graphite, diamond, graphene, CNTs, and fullerenes, have gained significant attention in PEC applications, particularly for hydrogen production through water splitting. Graphene, with its high specific surface area, superior electron mobility, optical transparency, and excellent electrical and thermal conductivity, stands out as a highly efficient material for photocatalytic and PEC applications. Graphene derivatives such as graphene quantum dots (GQDs), GO, and rGO further enhance PEC performance due to their tunable electronic properties and surface functionalization capabilities. Despite certain carbon-based materials lacking intrinsic photocatalytic properties, strategies such as surface modification, heterostructure construction, and elemental doping have been employed to enhance their activity.69–71
In recent years, PEC technology has shown immense promise for sustainable energy conversion, particularly in the production of green hydrogen via water splitting and the reduction of CO2 into valuable chemical feedstocks. The integration of nanostructured carbon materials with PESs is expected to drive further advancements, improving efficiency, scalability, and commercial viability for future clean energy applications. Continued research into material optimization and system design will be instrumental in developing next-generation PEC technologies for sustainable environmental and energy solutions.72
In particular, CNT-based composites, such as MoS2/CNT hybrids, exhibit improved photocatalytic efficiency and stability due to enhanced charge separation and extended light absorption into the visible range (>400 nm). Similarly, CdS/MoS2/CNT composites have demonstrated significantly higher photocurrent densities—approximately 12 times greater than pristine CdS, attributed to the role of CNTs as co-catalysts and charge transfer facilitators.74 Bismuth vanadate, a promising photoanode material, suffers from limited charge separation and transport properties. However, incorporating carbon nanomaterials, such as rGO and graphitic carbon nitride (g-C3N4 or gCN), enhances light absorption and surface porosity, thereby improving photocatalytic efficiency.75 gCN-based composites, particularly those engineered via defect modulation and heterojunction formation, have gained attention for their ability to enhance charge separation and conductivity. Transforming g-C3N4 from nanoplates to nanorods increases photocatalytic activity and photocurrent response under visible light by 1.5 and 2 times, respectively. Additionally, heteroatom doping (e.g., C, P-doped g-C3N4) has demonstrated a 9.7-fold enhancement in H2 production via photocatalytic water splitting.76–80
Carbon quantum dots (CQDs) have emerged as a new class of photocatalysts owing to their low toxicity, cost-effectiveness, long photoluminescence lifetimes, and resistance to photobleaching. Compared to metal-based counterparts, their exceptional photostability makes them suitable candidates for sustainable photocatalysis. Furthermore, the functionalisation of g-C3N4 with porphyrins has shown enhanced charge transfer and hydrogen evolution efficiency, while porphyrin/rGO nanocomposites have exhibited superior electron transfer and high photocatalytic activity under visible light irradiation.67,81
Overall, carbon-based photocatalysts offer significant potential for advancing PESs, particularly in wastewater treatment, hydrogen production, and CO2 reduction. Ongoing research in band gap engineering, surface functionalization, and nanostructured materials is expected to improve photocatalytic performance further and enable scalable, cost-effective applications in renewable energy and environmental remediation.
The carbon structure also plays a crucial role in extracellular electron uptake, especially in CO2 reduction on a photo-biocathode. In the rGO–SiO2–TiO2 heterojunction system, the introduction of rGO into the SiO2–TiO2 photocatalyst, was revealed as an electron transfer facilitator, assisted by its π–π conjugation effect. This mediation remarkably elevates the electron transfer rate between SiO2–TiO2 and rGO, enhancing electron transfer to hydrogen and direct transfer to microbes.82 PMECs represent an advanced class of MECs that incorporate photocatalysts at the anode, cathode, or both electrodes to facilitate semi-artificial photosynthesis.83,84 These hybrid systems leverage both biocatalysts (e.g., enzymes, microbes) and synthetic materials (e.g., semiconductors, electrodes) to drive complex and endergonic chemical reactions.85 Biocatalysts contribute to electrochemical transformations by enhancing selectivity and efficiency, whereas synthetic materials aid in immobilization, light absorption, charge transfer, and product separation. The integration of microbes and enzymes with electrodes provides a viable alternative to noble-metal-based catalytic processes, reducing dependency on scarce and expensive materials. Light, a sustainable source of renewable energy in PMECs, facilitates generation of charge carriers, which requires the carbon-based material to be photoactive, and after illumination of light, the subsequent steps are light absorption, charge transfer, redox reactions, adsorption, desorption and mass diffusion of chemical species and charge recombination, with all the sequential processes depicted in Fig. 4 for a typical particulate photocatalyst. TiO2 and SiO2 are widely used semiconductors. Incorporation of rGO into the SiO2–TiO2 semiconductor was recognized as a crucial element in enhancing its photocatalytic performance in a PMEC system, which is attributed to its large specific surface area. This modification broadened the light absorption range, thereby increasing the UV-Vis absorption intensity and providing additional active sites for photocatalytic reactions. Eventually, the interaction between rGO and light leads to an increased generation of charge carriers.82 Despite their promise, the practical implementation of photocatalysts in MECs presents several challenges. A significant issue arises from the generation of ROS, which inhibits hydrogen production at neutral pH (pH ≈ 7) and poses toxicity risks to microbial communities. Additionally, certain photocatalysts contain metal ions that may dissolve into the system, leading to contamination and performance degradation.54 To mitigate these effects, strategies such as controlling metal ion dissolution and employing carbon-based photocatalytic electrodes have been explored. In photo-electrochemical CO2 reduction applications, Cu2O nanowires have been investigated as photoanodes. However, their susceptibility to photo-corrosion, primarily due to self-reduction by photo-generated electrons, presents a major limitation.86 Tailoring the electrolyte conditions has been proposed as a potential strategy to alleviate photo-corrosion and enhance the stability of these materials. Addressing these challenges through material optimization and system design improvements is crucial for advancing PMEC technology toward scalable and sustainable applications. The development of efficient PMECs represents a promising step toward sustainable energy production and environmental remediation. However, addressing the limitations associated with photocatalyst stability, biocompatibility, and charge transfer efficiency remains crucial for advancing PMEC technology. Future research should focus on optimizing electrode materials, improving bioelectrode integration strategies, and designing scalable systems that can operate efficiently under real-world conditions. Through these advancements, PMECs have the potential to revolutionize hydrogen production, CO2 conversion, and wastewater treatment in an energy-efficient and environment-friendly manner.
| 2CO2 + 4H2 → CH3COOH + 2H2O |
| Electrochemical reaction | E 0 vs. SHE(V) |
|---|---|
| All the values of the above table have been taken from the literature.93–95 | |
| CO2 + e− → CO2˙− | −1.85 |
| CO2(g) + 2H+ + 2e− → HCOOH(aq) | −0.61 |
| CO2(g) + 2H+ + 2e− → CO(g) + H2O(l) | −0.52 |
| CO2(g) + 4H+ + 4e− → HCHO(aq) + H2O(l) | −0.48 |
| CO2(g) + 6H+ + 6e− → CH3OH(aq) + 4H2O(l) | −0.38 |
| 2CO2(g) + 12H+ + 12e− → C2H4(g) + 4H2O(l) | −0.34 |
| CO2(g) + 8H+ + 8e− → CH3COOH(aq) + 2H2O(l) | −0.28 |
| CO2(g) + 8H+ + 8e− → CH4(g) + 2H2O(l) | −0.24 |
| 2H+ + 2e− → H2(g) | −0.41 |
Methanogenesis is another prominent metabolic route, following the Wolfe cycle, in which hydrogenotrophic methanogens convert CO2 into methane. Hydrogen molecules (H2) serve as electron donors, facilitating CO2 reduction through hydrogen-mediated electron transfer, thereby enhancing methane production rates.96,97 The overall reaction carried out by the Wolfe cycle for CO2 reduction is:
| CO2 + 4H2 → CH4 + 2H2O (ΔG° = −130.7 kJ mol−1) |
MECs provide a superior alternative to photocatalytic and electrocatalytic CO2 reduction due to their ability to harness microbial activity for electrochemical reactions at low applied voltages (0.2–0.8 V). Additionally, their integration with wastewater treatment presents a promising “waste-to-value” approach. However, several challenges hinder their efficiency, including poor biocompatibility between electrodes and microbes and low electron transfer efficiency at the cathode. To address these limitations, researchers have explored novel carbonaceous cathodes, such as prussian blue nanocube-modified carbon felt (PBNC-CF), which function as artificial electron mediators. Studies have demonstrated that PBNC-CF-based cathodes achieved twice the biofilm thickness compared to unmodified carbon felt, leading to enhanced volumetric acetate production (0.20 ± 0.01 g L−1 day−1) in a 10 L MES.98 These advancements underscore the potential of engineered carbon-based electrodes in enhancing MEC's performance for sustainable CO2 reduction and biofuel production.
![]() | ||
| Fig. 5 A schematic diagram of a photo-microbial electrolysis cell (PMEC) illustrating the CO2 reduction. | ||
A dual-photoelectrode PMEC has been proposed, employing BiVO4–RuO2–IrO2 on a Ti mesh as the photoanode and ZIF-67/g-C3N4 on carbon felt as the photocathode to facilitate CO2 reduction to acetate. In this system, the anode remains abiotic, whereas the cathode is enriched with a mixed microbial culture. The dual-photoelectrode configuration enables the simultaneous generation of e−/h+ pairs upon light irradiation, improving charge transfer efficiency. The electrons generated at the photoanode compensate for the holes at the photocathode, enhancing system compatibility. To achieve water oxidation at the abiotic photoanode, its conduction band edge potential must be more negative than the H+/H2 redox pair, promoting efficient electron transport from the anode to the cathode. Simultaneously, the valence band edge potential should be sufficiently positive relative to the O2/H2O redox potential. The BiVO4–RuO2–IrO2/Ti photoanode, where RuO2–IrO2/Ti acts as a co-catalyst and supports the fabrication of BiVO4, facilitates water oxidation, leading to proton and electron generation along with oxygen evolution. Electrons migrate toward the cathode, while holes generated on BiVO4 (bandgap: 2.4–2.5 eV) upon visible light irradiation help overcome kinetic barriers associated with water oxidation.102 This process effectively prevents charge carrier recombination, ensuring enhanced performance. Both photoexcited electrons and those generated via water oxidation are transported through an external circuit to the cathode, while protons migrate through a proton exchange membrane. In the cathodic compartment, ZIF-67/g-C3N4 serves as the photocathode. ZIF-67, a metal–organic framework with high porosity and chemical stability, enhances CO2 adsorption, ensuring a consistent substrate supply. Meanwhile, g-C3N4 (bandgap ∼2.7 eV) contributes to efficient photogenerated electron–hole separation, a high specific surface area due to its intrinsic layered structure, and an extended π-conjugated system akin to graphene. Upon visible light irradiation, holes generated on g-C3N4 are compensated by electrons transferred from the anode, while photogenerated electrons from the photoanode are either directly transferred to microbes or mediated by H2, acting as an electron shuttle. This process leads to acetate production, achieving a yield of 6.93 g L−1.102 Further, a mesoporous rGO–SiO2–TiO2 (Z-scheme heterojunction) nanocomposite has been reported (Fig. 6) for efficient carbon dioxide reduction and high-performance supercapacitor applications. The incorporation of SiO2–TiO2 nanocomposites into rGO significantly improves charge transport, overall conductivity, electrode–electrolyte interaction, and reaction kinetics. When utilized as a cathode in a MEC with cultivated anaerobic bacteria, this system demonstrated 2.1 times higher photocurrents compared to a bare carbon felt electrode, achieving an acetate production rate of 3.21 mM day−1 with a coulombic efficiency of 78% and a current density of 2.7 A m−2.82 Another study investigated a photo-assisted MEC employing Serratia marcescens Q1 as an electrotrophic microorganism and a photocathode composed of graphite felt coated with g-C3N4 and decorated with WO3–MoO3 nanoparticle mixtures. The Z-scheme heterojunction of WO3/MoO3/g-C3N4 facilitated bicarbonate (HCO3−) reduction to acetate, yielding a photocurrent 4.8 times higher than that recorded with a g-C3N4 electrode alone and 2.1 times greater than that of WO3/MoO3 species. Upon light irradiation, the Z-scheme heterojunction generated long-lived e−/h+ pairs, where conduction band electrons of g-C3N4 reduced protons to H2, which was subsequently bio-assimilated by microbes for acetate production, while holes were neutralized by electrons transferred from the anodic chamber.103 For enhanced acetate synthesis from bicarbonate (HCO3−) in photo-assisted microbial electrosynthesis (MES), a Z-scheme Ag3PO4/g-C3N4 photocatalytic heterojunction was proposed. When coupled with the non-photosynthetic bacterium Serratia marcescens Q1, this system achieved an acetate production rate of 5.4 mM day−1, with a coulombic efficiency of 93% at a current density of 3.3 A m−2.104 Similarly, an innovative CuO/g-C3N4/rGO photocatalyst-based cathode, when combined with a mixed microbial culture, facilitated CO2 reduction, producing acetate at a rate of 0.27 g L−1 day−1 at a potential of −0.9 V (versus Ag/AgCl). The inclusion of rGO in CuO/g-C3N4 improved light absorption capacity and enhanced photogenerated electron–hole separation and migration efficiency compared to CuO/g-C3N4 alone.105 A Z-scheme heterojunction, α-Fe2O3/g-C3N4, was proposed as a photocathode for a photo-assisted MEC, where the system exhibited enhanced photogenerated electron–hole separation under visible light, achieving an acetate production rate of 0.33 g L−1 day−1 from CO2 reduction, which was three times higher than that of a carbon felt cathode.106 Additionally, a CoP-Fe2O3/C3N4 photocathode was developed for the reduction of CO2 into polyhydroxybutyrate (PHB) in an MES system utilizing Ralstonia eutropha as a biocatalyst. This photocathode integration facilitated charge carrier separation, providing additional reducing power for CO2 conversion. The system yielded 87.54 mg L−1 of PHB at −1.05 V, approximately three times higher than that obtained with a carbon felt electrode. At −0.9 V, PHB production further increased to 142.20 mg L−1.107 Recent advancements have demonstrated that PBESs can serve as efficient platforms for H2 generation utilizing carbon-based photocatalysts in conjunction with biocatalysts. In another study, a PBES was designed for CO2 reduction using a carbonaceous material as a supportive base, integrating NCW-g-C3N4/ACF and g-C3N4/ACF as bioanodes, with Escherichia coli derived from wastewater acting as a biocatalyst. This system synthesized approximately 12.8 mM of formate per day under visible light irradiation. The 2D structure of g-C3N4 in the biocathode facilitated efficient charge carrier transport between the bacteria and substrate, while ACF served as a supportive material, offering high biocompatibility, electrical conductivity, and surface area. In the photoanode, g-C3N4, a metal-free semiconductor with a bandgap of ∼2.7 eV, exhibited a high charge recombination rate, whereas Ni or Co metal tungstate possessed a relatively higher bandgap and lower charge recombination rate. The integration of these materials resulted in the formation of a Z-scheme heterojunction, effectively mitigating the limitations of each component.28 Overall, the photocatalyst plays a crucial role in generating highly reactive excited electrons, facilitating redox reactions, while the biocatalyst efficiently utilizes these electrons to produce value-added products according to their metabolic pathways. The integration of advanced photocatalytic materials and microbial electrocatalysis in PMECs underscores their potential for sustainable CO2 conversion and bioenergy generation, addressing critical environmental challenges through innovative technological solutions.
![]() | ||
| Fig. 6 Photo-reduction mechanism of CO2 to acetate using a mixed culture via the utilization of an rGO-doped SiO2–TiO2 heterojunction in MES. Reprinted with permission.82 Copyright 2023, Elsevier. | ||
Anodic chamber:
| CH3COO− + 4H2O → 2HCO3− + 9H+ + 8e− |
Cathodic chamber:
| 8H+ + 8e− → 4H2 |
Overall reaction:
| CH3COO− + 4H2O → 2HCO3− + H+ + 4H2 |
Acetate is considered as the most efficient substrate for microbial oxidation in MECs, leading to enhanced hydrogen production. Under standard biological conditions, the anodic potential (Ean) is reported as −0.279 V, while the cathodic potential (Ecat) is approximately −0.414 V. The equilibrium potential (Eeq) for the reaction is calculated as −0.14 V. However, to drive hydrogen evolution effectively, an external voltage between 0.2–1.0 V is typically applied due to electrode overpotentials in real MEC systems.108 Despite these applied voltage requirements, hydrogen production in MECs is preferred over conventional electrochemical water splitting. This is because traditional electrolysis requires a significantly higher applied potential (>+1.23 V) under standard conditions (25 °C, 1 atm), regardless of the electrolyte used.109 The lower energy input required in MECs makes them a promising alternative for energy-efficient biohydrogen generation while simultaneously mitigating wastewater pollution.
![]() | ||
| Fig. 8 (A) H2 generation in a PMEC. Reprinted with permission.116 Copyright 2017, ACS. (B) Schematic diagram of photogenerated electron–hole pair transfer and H2 production in a typical PMEC with a bioanode and photocathode. (C) Illustration of electron transfer on the anode-microbe interface. (D) Mechanistic sketch of electron transfer and H2 production in an AgInS2/In2S3@E. coli semiconductor-biohybrid system. Reprinted with permission.114 Copyright 2021, Elsevier. | ||
The mechanism of generation of charge carriers, and their fate and interaction at the bio-electrode interface can be explained more efficaciously using the example of a carbon-based photo-bio electrode either as a photo-bioanode (Fig. 8C) or photo-biocathode (Fig. 6 and 8D). In the case of photo-biocathodes, in a PMEC, light illumination results in the generation of e−/h+ pairs, e− migrate to the cathode via an external circuit and meanwhile, there is manifestation of a microbial oxidation reaction that also results in the generation of e− (acetate oxidation needs only ∼–0.3 V potential whereas oxidation of H2O demands ∼0.8 V potential to generate e−), and these e− are responsible for compensation of h+ in the valence band of the photocatalyst. Thus, the photocatalyst facilitates an additional electron source, and heightens the system's overall efficiency, surpassing the performance of MECs.114,115
In the case of photo-biocathode, enlightenment excites the e− to the conduction band, leaving behind h+ in the valence band. These photogenerated electrons are transported to microbes to facilitate the metabolic reduction reaction through their conductive pilli, membrane protein (cytochrome c) or exogenous electron shuttles, and occasionally H2 act as a mediator to transfer electrons between microbes and electrodes. Photogenerated holes also play a significant role as in the rGO–SiO2–TiO2 photo-bio-cathode it was revealed that h+ serves as an additional driving force that effectively traps the electrons in the external circuit, resulting in increased current generation, in the presence of KI as a hole scavenger, a reduction in acetate production rate from 3.2 ± 0.16 mM day−1 to 2.10 ± 0.1 mM day−1 was observed. Besides the synergistic relation between microbes (waste) and light, the carbon-based photoactive electrodes offer a better environment and stage for their growth and survival, so in cutting-edge research, there is inciting competition to develop PMECs with carbon-based electrodes.82
In a separate study, a single-chambered PMEC system utilizing a ZnFe2O4/g-C3N4 photocathode and graphite felt as the anode material demonstrated the exclusive production of H2 without the generation of CH4 and CO2, achieving a production rate of 1.70 ± 0.04 m3 m−3 day−1. The integration of ZnFe2O4 (bandgap: 1.90 eV) with the carbonaceous material g-C3N4 (bandgap: 2.70 eV) effectively reduced the overall bandgap of the photocathode and minimized charge recombination.
Additionally, a single-chambered MEC incorporating a dual bioelectrode configuration was reported, where ZnFe2O4/g-C3N4 cathodes facilitated efficient and exclusive H2 production at a rate of 0.11 ± 0.01 m3 m−2 day−1 and 1.70 ± 0.04 m3 m−3 day−1. This system exhibited a solar-to-hydrogen conversion efficiency of 4.08 ± 0.17% and an energy efficiency relative to electrical input of 233 ± 5%. The structured ZnFe2O4/g-C3N4 cathodes demonstrated significantly higher photocurrents compared to the individual components (4.3-fold increase over g-C3N4 and 3.3-fold over ZnFe2O4). Furthermore, after four operational cycles, the system exhibited negligible Fe and Zn leaching, indicating the cathode's structural stability and long-term durability.117 The UV-Vis DRS spectra of ZnFe2O4, g-C3N4, and ZnFe2O4/g-C3N4 revealed distinct absorption edges corresponding to their intrinsic Eg. Specifically, g-C3N4 exhibited an absorption edge at approximately 450 nm, aligning with its reported Eg of 2.70 eV, while ZnFe2O4 showed broad absorption within the 350–650 nm range, consistent with its Eg of 1.90 eV. The Mott–Schottky plots of ZnFe2O4 and g-C3N4 demonstrated positive slopes in the linear regions, confirming their n-type semiconducting nature. The ECB determined from these plots was −0.35 eV for ZnFe2O4 and −1.2 eV for g-C3N4, whereas the corresponding EVB values were reported as 1.55 eV and 1.50 eV, respectively. These findings indicate the formation of an n–n heterojunction at the photocathode interface. Upon light irradiation, the photo-excited electrons migrated from g-C3N4 to ZnFe2O4, driven by the more negative ECB of g-C3N4, whereas the holes moved in the opposite direction, from the more positive EVB of ZnFe2O4 to g-C3N4. This directional charge transfer significantly enhanced charge separation efficiency, minimized electron–hole recombination, and improved the photocatalytic activity of the system. MEC was measured as a key route for biological H2 generation, although PMEC can be recognized as a more advanced version as a comparative study was reported for H2 evolution in the system with a bioanode made of carbon fiber brush and when Pt as a cathode is used at 0 bias conditions in a MEC, it resulted in almost zero current density while at 0.8 V bias, it only produced 1 mA cm−2 current density; on the other hand, the same bioanode with GaInP2–TiO2–MoSx as a photocathode in a PMEC recorded a >10 mA cm−2 current density.116
![]() | ||
| Fig. 9 Schematic representation of the typical MFC principle with inclusion of photocatalysis at either/both ends, photo-bioanode and photocathode. | ||
The diversity and resilience of microbial communities, characterized by their high reproductive capacities and ability to thrive under mild environmental conditions, make them ideal for sustained, long-term operation in PMFCs. Adequate illumination is a crucial environmental factor for optimal PMFC performance. Unlike photo-driven PFCs, where operation is limited by light availability, the use of electrogenic microorganisms on anodes ensures the stable operation of PMFCs even in low-light or dark conditions. When photocatalysts are incorporated into the cathode of an MFC, hole–electron pairs are generated upon light irradiation. The photogenerated holes interact with electrons arriving from the anodic chamber, while the photogenerated electrons readily react with electron acceptor species at the cathode. This mechanism effectively suppresses the recombination of e−/h+ pairs, thereby improving photocatalytic efficiency. Moreover, a major limitation in MFCs is the high cathodic overpotential and slow reaction kinetics of cathodic reduction reactions, which restrict large-scale application. The introduction of a cathodic photocatalyst not only enhances pollutant degradation (e.g., dye removal) but also accelerates cathodic reaction kinetics, thereby overcoming the high cathodic overpotential. Photocatalytic processes have the capability to break down complex organic compounds into simpler, less harmful molecules, which can then be biodegraded more efficiently by microorganisms. It has been demonstrated that photocatalytic oxidation serves as an effective pre-treatment strategy before biodegradation, as it enhances the bioavailability of recalcitrant pollutants. Although photodegradation is generally more efficient and rapid than biodegradation for stubborn contaminants, it often leads to partial degradation rather than complete mineralization.122,123 Additionally, the rapid recombination of photogenerated e−/h+ pairs limits the overall photodegradation efficiency. Therefore, the integration of photocatalysis with MFCs has gained significant attention, as it combines microbial metabolism with photocatalytic processes for enhanced wastewater treatment and bioenergy generation. In PMFC configurations, photocatalysts can be incorporated either as a photoanode or photocathode. Most reported studies have focused on dual-chamber configurations, where bioanodes are coupled with photocathodes, or biocathodes are combined with photoanodes. This arrangement ensures an efficient electron transfer pathway, enhanced degradation of pollutants, and improved bioelectricity generation, making PMFCs a promising hybrid system for sustainable energy production and environmental remediation.124
The research community has increasingly focused on carbonaceous electrode materials, particularly bamboo charcoal (BC), due to its high specific surface area, exceptional electrochemical stability, cost-effectiveness, and superior ORR activity. A multi-cathode PFC system, employing a TiO2 photoanode and a BC/Ti cathode, demonstrated superior methyl orange (MO) degradation efficiency and higher bioelectricity generation compared to conventional single-cathode PFC designs.134,135 A research study gave excellent results regarding degradation of Ciprofloxacin by a Zn–Al mixed metal-oxide (MMO)/rGO nano composite under visible light, which was 3 and 4.6 times greater than zinc–aluminium layered double hydroxide and zinc–aluminium MMO, respectively. It was attributed to response to broad range of visible light that they showed such great efficiency. Upon further comparison with TiO2, nanocomposites of rGO–Fe3O4/TiO2 showed 98.99% degradation in only 55 minutes of visible light irradiation, while TiO2 degraded 67% of the same in 120 minutes. Such increment of the result was wheeled by greater surface area of Fe3O4 and rGO in the nano composites, which provides TiO2 with more active sites for catalysis.136 For the degradation of reactive green 19 (RG19), a membraneless PFC system was developed using a zinc oxide/carbon (ZnO/C) photoanode and a platinum/carbon (Pt/C) cathode. This setup was designed to evaluate the impact of dissolved oxygen (DO) concentrations on dye degradation and bioelectricity production.137 Experimental results revealed that higher DO levels significantly enhanced the degradation efficiency of diazo dyes and boosted electricity output. In a parallel study, ZnO was immobilized onto a Zn-based photoanode, paired with a Pt-loaded carbon cathode, where DO played a crucial role in prolonging e−/h+ pair separation in ZnO. This process led to improved degradation efficiency of RG19.138 Notably, the degradation rate of RG19 was found to be higher than that of acid orange 7, primarily due to the presence of electron-donating triazine (–NH–) functional groups in RG19, which facilitated its oxidative decomposition. Moreover, an integrated PFC system incorporating periodate activation was designed using a rGO/TiO2 nanotube (NT) photoanode and a polypyrrole (Ppy)/MWCNT cathode. This system achieved an unprecedented maximum acid red 14 degradation efficiency of 99%, with citric acid employed as an effective co-catalyst to enhance electron transfer dynamics.139 A PFC system incorporating a nanostructured BiVO4 film and an Au-decorated, commercially available buried junction silicon photoanode was constructed. This novel system exhibited high-efficiency energy conversion and accelerated MO degradation. The introduction of a small amount of sulfite along with sufficient oxygen in the reaction chamber further enhanced bioelectricity generation and organic pollutant degradation, demonstrating the feasibility of integrating advanced photocatalytic-electrochemical approaches in MFC technology.140 These findings underscore the immense potential of carbon-based PMFCs in achieving dual-purpose applications of bioenergy generation and wastewater treatment. A study exhibited improved electron utilization upon using bi-anodes in MFCs having TiO2/Fe2O3 as a photoanode and another, as a bioanode integrated with a solar cell.141 The microbial oxidation and photo-electrocatalysis were significantly accelerated with dual-anode MFC to carry out enhanced electron transfer to the external circuit.142 The incorporation of doping strategies, hybrid catalyst architectures, and advanced carbon-based electrode materials has led to significant enhancements in photocatalytic efficiency, charge transport properties, and overall system stability. Moving forward, future research should focus on integrating nanostructured materials, optimizing charge transfer mechanisms, and developing scalable designs that facilitate real-world deployment of bioelectrochemical energy systems. By synergistically combining microbial electrochemical activity with advanced photocatalytic processes, PMFCs offer a sustainable pathway for clean energy production and environmental remediation.123,124
| Material type | Cathode | Microbial inoculum | Electrode fabrication method | System (MEC/MFC/PEC/PMEC) | Product | Applied potential (V) | Power density (W m−2)/current density (A m−2) | Stability | COD removal | Coulombic efficiency/faradaic efficiency (%) | Ref. |
|---|---|---|---|---|---|---|---|---|---|---|---|
| Metal-based | Si-nanoarray | Sporomusa ovata | — | Photo-biohybrid system | Acetate | 0.2 | 3 | 200 h | — | 90 | 143 |
| Carbon-based | Carbon cloth | Methanogen | Hydrothermal | Hybrid PMEC | CH4 | −0.3 | 0.35 | 90 h | — | 95.2 ± 1.8% | 144 |
| Carbon-based | Carbon cloth | E. coli | Hydrothermal | MFC | ORR | — | 1.964 | — | — | — | 145 |
| Metal oxide-based | GaInP2–TiO2–MoSx | Anaerobic sludge | Vapour phase epitaxy, reductive electrodeposition | PMEC | H2 | 0, 0.8 | 4.2, ∼100 | 24 h | — | >93 | 116 |
| Doped ceramic-based | rGO/WO3/carbon cloth | Mixed culture | Electrospinning | MEC | Acetate | −0.5 | 13.56 ± 0.5 | — | — | 86 ± 1.0 | 146 |
| Conducting polymer-based | Carbon cloth | Chitosan | SILAR method | Hybrid PMEC | CH4 | −0.7 | 0.375 | — | — | 94.4 | 147 |
| Metal oxide-based | LaCoO3 | Shewanella species | Sol–gel method | MFC | ORR | — | 0.0139 | — | — | — | 148 |
| Metal oxide-based | Co0.5Cu0.5 Bi0.1Fe1.9O4 | Synthetic wastewater+ sludge | Sol–gel auto-combustion | MFC | ORR | — | 11.44 | 50 cycles | — | 21.4 | 149 |
| Conducting polymer-based | Nickel-phthalocyanine/MnO2 | Mixed culture | Hydrothermal | MFC | ORR | — | 8.02 ± 0.38 | — | 80.3 ± 3.8 | 27.9 | 150 |
![]() | ||
| Fig. 10 Advantages of PMECs for organic and inorganic pollutant degradation and sustainable energy production. | ||
| Cathode/photocathode | Anode/photoanode | Band gap of photoelectrode (eV) | Potential (vs. Ag/AgCl) | Biocatalyst | Product | Production rate | Coulombic efficiency/faradaic efficiency(%) | Current density(A m−2) | Ref. |
|---|---|---|---|---|---|---|---|---|---|
| rGO–SiO2–TiO2 | Carbon felt | — | — | Mixed culture | Acetate from inorganic carbon | 3.21 mM day−1 | 78 | 2.7 | 82 |
| WO3/MoO3/g-C3N4 | Carbon rod | 2.56 | −1.3 | Serratia marcescens | Acetate from inorganic carbon | 3.12 ± 0.20 mM day−1 | 73 ± 4% | 2.5 ± 0.3 | 103 |
| CuO/g-C3N4/rGO | Ti-mesh coated with Ru and Ir | 2.21 | — | Mixed culture | Acetate | 0.27 g L−1 day−1 | — | 14.8 | 105 |
| ZIF-67/g-C3N4 on carbon felt | BiVO4–RuO2–IrO2 on Ti mesh | 1.95, 2.12 | −0.9 | Mixed culture | Acetate | 0.46 g L−1 day−1 | — | — | 102 |
| Ag3PO4/g-C3N4 | Carbon rod | 2.3 | −1.3 | Serratia marcescens | Acetate from inorganic carbon | 5.4 mM day−1 | 93 | 3.3 | 104 |
| α-Fe2O3/g-C3N4 | Ru/Ir–Ti mesh | — | −0.9 | Mixed culture | Acetate | 0.33 g L−1 day−1 | — | −13.5 | 106 |
| CuO/g-C3N4 | Ru/Ir–Ti mesh | — | — | Mixed culture | Acetate | 0.16 g L−1 day−1 | — | −114 | 105 |
| CoP–Fe2O3/C3N4 | Ru/Ir–Ti mesh | — | −0.9 | Ralstonia eutropha | Polyhydroxybutyrate | 0.02 g L−1 day−1 | — | — | 107 |
| Graphitic-C3N4/ACF | NCW-gCN/ACF | ∼2.80 eV, ∼2.66 eV | −1.0 | E. coli | Formate | 12.8 mM day−1 | ∼57 | 0.64 | 28 |
| CDs/g-C3N4 | Graphite felt | — | 0.8 | — | H2 | 0.1138 m3 m−3 day−1 | — | — | 111 |
| CeO2–rGO/carbon film | CeO2–rGO/carbon film | — | 1 | Mixed culture | H2 | 5 m3 m−3 day−1 | 95 | — | 70 |
| g-C3N4/CQDs/BiOBr | Pt/C-carbon brush | ∼2.74 | 0.8 | Mixed culture | H2 | 0.02967 L L−1 day−1 | — | ∼10 | 151 |
| ZnFe2O4/g-C3N4 | Graphite felt | — | 0.6 | Mixed culture | H2 | 1.70 ± 0.04 m3 m−3 day−1 | — | — | 117 |
![]() | ||
| Fig. 11 A 3D-barchart showing the yield of acetate, formate, PHB and H2 in a PMEC system with carbon-based photoelectrodes. | ||
Scaling up often reveals that the power output does not increase proportionally with the volume of the anodic chamber or the electrode surface area. The primary limitations in larger MFCs arise from electrochemical thermodynamics, electrode reaction kinetics, and mass transport constraints, which restrict the system's power production. High overpotentials and reduced coulombic efficiency limit the scalability of a single MFC. Therefore, electrode materials with low-cost catalysts are needed to reduce activation overpotentials and improve coulombic efficiency, making MFCs more viable for field applications. MFCs offer notable advantages, such as non-conventional green electricity generation, powering underwater sensors, remote sensing, biological oxygen demand monitoring, hydrogen production, and wastewater treatment. However, several challenges persist, including membrane biofouling, pH splitting, oxygen diffusivity, membrane internal resistance, production costs, and lower power output. To enhance the power output and make MFCs more practical, it is necessary to minimize activation overpotentials at both the anode and cathode by developing more efficient yet cost-effective electrode materials.8,9 Additionally, reducing ohmic losses due to electron flow resistance at the electrodes and ion flow resistance in the membrane is essential. Strategies such as decreasing electrode spacing, using more conductive electrode materials with coatings, and selecting ion-conductive membranes with lower resistance can help address these losses.152 Replacing costly membrane separators with ceramic separators modified with cation exchangers to improve proton conductivity could also reduce costs.153 Commercializing MFCs will depend on using catalyzed electrodes that support higher current densities, thus enabling larger anodic chamber volumes and maximizing energy extraction while treating wastewater.8,9Table 6 is an account of the comparative performance of different PMFCs. Recent advancements in nanomaterials have led to innovative hetero-nanostructures for solar water-splitting, with photocurrents ranging from microamperes to milliamperes per square centimeter. This progress has been widely reviewed, with a focus on fabrication techniques and improvements in large-bandgap semiconductors like TiO2 and ZnO, which show strong performance in solar water-splitting. New systems, such as oxynitrides, tantalates, and niobates, also show promise.154 Nowadays, photo-bioelectrofenton systems are mostly prevalent in batch-mode, but it is continuous-mode which makes up for much more stability in electron utilization when applied in practical industrial conditions. Previous studies have taken up organic loading rate (OLR) and hydraulic retention time (HRT) as two major parameters to keep note of electron flow in continuous flow mode systems. In a bi-chambered system, pharmaceutical wastewater was continuously flowed into the anodic chamber through a peristaltic pump and the operated effluent, treated wastewater was sent to be a clarifier, again continuously, where after the settlement of sludge by gravity, the suspended liquid was transported to the cathodic chamber where it took part in reaction. This operated system showed OLR of 0.58 g L−1 day−1, HRT equalling 83.33 h, COD removal efficiency of 93% and coulombic efficiency equal to 5.36%.155 In another study, a 20 L reactor was set up in continuous mode to incur industrial-level research where methylene blue (MB) was degraded from operated wastewater with a decolorization efficiency of 99% at 28 h HRT.156 This study exhibited a scaled-up industrial level continuous-flow mode wastewater treatment system for real world application successfully. A study displayed a continuously fed bio-electric Fenton system for the decomposition of metoprolol with the rate of 77%, 92%, and 95% with respect to 2, 4, and 6 h HRT, respectively.157 This research clearly showed how hydroxyl radicals generated during the reaction get cleansed out through the effluent at shorter HRT in a continuous-flow system, while as the HRT is significantly increased, they ought to react and take part in the reaction. The above-mentioned research about continuous mode systems demonstrated a variety of pros over batch mode systems indicating better coulometric efficiency and higher operational efficiency with excellent stability and great ease in operability, plus control over microbial metabolism, and repeatability at the economic level.158 MFCs present a sustainable approach to wastewater treatment, which is typically energy-intensive and costly. Traditional treatment methods do not generate revenue or add value to the treated water. Sustainable wastewater treatment processes are essential to addressing energy scarcity, resource depletion, and pollution. These processes aim for minimal resource consumption, neutral energy operation, consistent treatment performance, high-quality effluent for reuse, balanced investment, strong social equity, and low environmental impact.123,124 MFCs and MECs offer a cost-effective alternative by utilizing microorganisms as biocatalysts for organic matter oxidation and electron transfer to the anode for bioelectricity production. The performance of MFCs is influenced by electrochemical reactions at the anode and cathode, where methane or hydrogen may be produced, depending on the requirements. Carbon-based materials such as graphite and CNTs are commonly used due to their affordability, conductivity, and abundance.9 CNTs, despite issues with biotoxicity and biodegradability, have excellent mechanical, thermal, and electrical properties.170 Molybdenum and stainless steel are also used as anode materials, with molybdenum exhibiting high durability and corrosion resistance and stainless steel offering a high nickel content.171 For example, stainless-steel brushes used as cathodes have achieved hydrogen production rates of 1.7 m3 m−3 day−1, with an efficiency of 84%.172 One of the main limitations of MFCs is the reduction of molecular oxygen at the cathode, which increases potential losses. Despite the use of various catalysts at the cathode, oxygen reduction remains a key bottleneck. This issue can be addressed by increasing the cathode surface area and employing biological catalysts. The industrial scalability of MFCs for energy production and wastewater treatment is hindered by electrode material instability. Further research is needed to couple energy-harvesting systems with MFCs, potentially allowing for voltage storage and enhanced output during wastewater treatment. Cost reduction, improved harvesting efficiency, and design optimization are crucial for the sustainable development of MFCs, which could be integrated into self-powered energy-harvesting systems.8,9,122,123 MFCs being an impactful resource of green life are highly applicative and performative and the same is exhibited in Fig. 12.
| Anode/photoanode | Cathode/photocathode | Performance | Application | Ref. |
|---|---|---|---|---|
| Where Pmax represents maximum power density, Jsc – short circuit current density, Voc – open circuit voltage, J – current density,TOC is total organic carbon and RB5 is commonly abbreviated for reactive black 5 dye. | ||||
| ZnO/carbon felt | Pt/C | P max = 2.34 μW cm−2, Jsc = 0.0069 mA cm−2, Voc = 1000 mV | Degradation of Azo dye RB5 (13.6% at anode and 8.7% at cathode) | 159 |
| Carbon felt | Bi–TiO2/Vulcan AC/carbon-felt | P max = 224 mW m−2, COD removal efficiency = 78–89% | Visible light irradiation photocatalytic activity | 160 |
| Fe-graphene oxide-titanium phosphate | ZnIn2S4 | 90% removal of rhodamine B at pH 1, cell voltage = 0.4 V | Degradation of rhodamine B | 125 |
| NiFe layered double oxide/TiO2 | Carbon black | P max = 169 μW cm−2, Jsc = 1093 μA cm−2, Voc = 0.78 V | Electricity generation with hydrogen peroxide production | 161 |
| Ag–TiO2 | Pt/C on carbon cloth | P max = 1.85 W m−2, COD removal efficiency = 14.8% | Coulombic efficiency of 9.4% generates electrical power from the remediation of wastewater | 162 |
| WO3/W | Fe@Fe2O3/carbon felt | J sc = 0.59 mA cm−2, Pmax = 0.34 mW cm−2 | Wastewater decontamination and electricity generation | 132 |
| CdS–ZnS–TiO2 | Pt black on carbon black coated carbon paper | P max = 1.01 mW cm−2, Jsc = 2.1 mA cm−2, Voc = 1.07 V | Simultaneous organic compound degradation and electricity generation | 163 |
| Stainless steel/α-Fe2O3/carbon | Carbon felt disk | J = 46,500 mA m−2 | Photo-electrochemical interaction for high current output | 164 |
| N-doped graphene aerogel | Cu2O/Au nanowire | P max = 2849.9 mW m−2, J = 6500 mA m−2 | Efficient power output | 165 |
| Graphite rod | Co–N@MoS2/C | LEV degradation rate = 4.9 × 10−2 min−1, H2 evolution rate = 3.1 × 10−3 m3 m−3 min−1, J = 60 000 mA m−2 |
Levofloxacin remediation and energy catalysis | 166 |
| Carbon brush | Carbon cloth | CO2 fixation rate = 1292.8 mg L−1 day−1, Pmax = 5.94 W m−3, J = 441.75 mA m−2 | CO2 fixation and bioenergy generation | 167 |
| Ag3PO4-coated carbon cloth + TiN coated carbon cloth | Carbon brush | P max = 2.90 W m−2, COD removal efficiency = 83.21%, TOC removal efficiency = 72.47% | Synergistic effect of photo- and bio-degradation resulted in decolourization efficiency of 95.8% MB | 168 |
| Graphite plate | AgBr/ZnO-modified graphite | P max = 53.8 mW m−2 upon visible light irradiation and 32.5 mW m−2 in dark conditions | AgBr/ZnO-modified graphite resulted in 61% RB5 dye degradation over 72 h compared to bare graphite output of 11.74% | 169 |
![]() | ||
| Fig. 12 As an innovative solution, MFCs promise to lead us toward a greener and more efficient future. | ||
Despite substantial progress in the development of microbial fuel cells and microbial electrolysis cells for wastewater treatment and bioenergy generation, several challenges still hinder their commercialization and large-scale implementation. A major limitation is their poor scalability, as the power output does not increase proportionally with the expansion of the anodic chamber volume or the electrode surface area. This issue primarily arises from constraints related to electrochemical thermodynamics, the kinetics of electrode reactions, and mass transport, all of which restrict overall system performance.
To develop MFCs and MECs for field-scale applications, it is necessary to overcome these limitations and improve energy efficiency. One of the key issues is the presence of high energy losses and low conversion efficiency, which directly reduce the electrical output and operational performance of these systems. Elevated energy losses at both the anode and cathode lead to decreased efficiency, while low conversion efficiency limits the ability of the system to generate electricity from the oxidation of organic matter. Therefore, identifying low-cost, high-performance electrode materials with efficient catalytic properties is essential to minimize energy losses and enhance the system's viability in real-world applications.
Another major challenge is the internal resistance within the system. Electrical resistance at the electrodes and ion transport resistance through the membrane reduce the overall voltage output. Addressing this issue involves decreasing the distance between electrodes, improving the conductivity of electrode materials through surface modifications, and selecting membrane materials with superior ion transport properties. Modified ceramic membranes incorporating cation exchangers have shown potential as affordable alternatives to traditional membranes by enhancing ion conductivity and reducing system costs. However, challenges such as membrane fouling, variations in acidity and alkalinity, oxygen diffusion, and internal resistance remain critical barriers to performance, particularly in large-scale applications.
Mitigating these issues requires the design of improved membranes that resist biological fouling, better control of acidity and alkalinity, and enhanced oxygen transport mechanisms. Despite these obstacles, microbial fuel cells and microbial electrolysis cells hold substantial promise in a wide range of applications, including decentralized electricity generation, wastewater treatment, power supply for remote sensors, monitoring of biological oxygen demand, and hydrogen gas production. Continued innovation in electrode materials and catalytic systems is expected to broaden the applicability of these technologies, especially in decentralized and environmentally sustainable wastewater treatment systems. A promising approach is the development of photoelectrochemical biohybrid systems, which integrate semiconductor materials with biological elements such as enzymes or whole-cell microorganisms. In these systems, light energy generates charge carriers within the semiconductor. The resulting electrons are transferred to the biological components, initiating biochemical reactions. These systems offer the potential to simultaneously treat pollutants and generate energy by leveraging solar energy and biologically driven processes. For instance, recent developments have demonstrated the effectiveness of combining carbon cloth biocathodes with titanium dioxide photoanodes to achieve direct electron-driven conversion of carbon dioxide to methane, with an energy efficiency of approximately 95% and minimal energy losses, as shown in Fig. 13. However, titanium dioxide's wide energy band gap restricts its ability to absorb light to ultraviolet wavelengths and makes it susceptible to chemical degradation under light exposure.173 To address these limitations, graphitic carbon has emerged as a promising material. It is abundant, chemically stable, and can be engineered to work with semiconductors that have lower energy band gaps (tandem strategies). This combination improves light absorption and charge transfer while reducing degradation, making carbon-based materials essential in the development of robust and efficient photoelectrochemical biohybrid systems. Scaling up microbial fuel cells and microbial electrolysis cells from laboratory or pilot setups to industrial applications presents several technical and economic challenges. Once again, the power output does not scale proportionally with the size of the anodic chamber or the electrode surface area due to the same underlying limitations in transport, kinetics, and thermodynamics. Cost is a significant hurdle as well, and using expensive materials like platinum and palladium in photo-bioelectrochemical systems is not feasible for large-scale deployment. Developing affordable, durable, and high-performance electrode materials is, therefore, a top priority. While carbon-based nanomaterials such as graphite and carbon nanotubes offer good electrical conductivity and affordability, concerns regarding their long-term stability and potential biological toxicity must be addressed. In microbial electrolysis cells, the biological process that produces methane competes with hydrogen gas production, reducing efficiency.144 Operational conditions and the type of organic material used influence this competition. Additional operational challenges such as membrane fouling, oxygen diffusion limitations, and internal resistance further impact system efficiency and scalability. From an industrial perspective, these factors contribute to higher costs and increased complexity.
![]() | ||
| Fig. 13 A Microbial-photoelectrochemical hybrid system depicting mechanism (A) and performance (B) outlining up to 96% faradaic efficiency for methane production via direct electron transfer-driven CO2 reduction. Reprinted with permission.144 Copyright 2018, Elsevier. | ||
Integrating MFCs and MECs with renewable energy sources, such as solar or wind power, could significantly improve their sustainability by reducing reliance on external electricity. For instance, photocatalysis along with wastewater treatment plants is found to utilize 1.4 US$ per hour at 10 mA cm−2 current density, which is far less than conventional systems. However, such integration requires the development of efficient energy management systems and energy storage technologies to ensure reliable operation. Moreover, such commercial projects make use of noble metals, whose processing gives negative eco impact.174 Long-term stability and durability are crucial for practical use. Electrode degradation due to corrosion, fouling, or mechanical stress remains a significant barrier. Materials like stainless steel and molybdenum offer promise due to their corrosion resistance and mechanical strength. Additionally, strategies to prevent biological fouling on electrode surfaces can help extend system lifespan and improve performance. The transition from laboratory research to real-world industrial use will depend on the development of scalable, low-cost methods for synthesizing, modifying, and fabricating electrode materials. One promising approach involves the use of biomass-derived materials, which offer high surface area, good electrical properties, and biological compatibility for microbial attachment and electron transfer. Combining microbial fuel cells with renewable energy systems could allow for simultaneous hydrogen production and wastewater treatment, an important step toward realizing circular economy. However, the cost of photovoltaic components and the lack of effective energy storage solutions must be resolved to make this hybrid approach feasible. In conclusion, while microbial fuel cells and microbial electrolysis cells face numerous challenges, their potential for sustainable energy production and wastewater treatment makes them a compelling area of research. Addressing the technical, economic, and environmental issues outlined above is essential to fully realize the promise of these technologies on an industrial scale.
Despite these advances, challenges such as membrane biofouling, pH splitting, oxygen diffusivity, electrode instability, and cathodic oxygen reduction remain. This review also identifies the need for durable electrode materials and low-cost, scalable synthesis processes suitable for real-world applications. There has also been discussion referring to the potential of nanomaterials, energy-harvesting systems, and emerging membrane technologies as avenues for overcoming these hurdles.
By synthesizing knowledge across multiple disciplines, this review offers a comprehensive roadmap for advancing PBESs. It also serves to guide future experimental and industrial efforts aimed at scaling up photocatalytic fuel systems for wastewater treatment and sustainable energy production. We hope that this work will contribute meaningfully to the ongoing discourse and inspire new strategies in the pursuit of global renewable energy and environmental goals.
Footnote |
| † Authors contributed equally. |
| This journal is © The Royal Society of Chemistry 2025 |