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Perspective—Trends in the Miniaturization of Photosynthetic Power Cell towards Improved Power Density

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Published 1 December 2022 © 2022 The Author(s). Published on behalf of The Electrochemical Society by IOP Publishing Limited
, , Citation Ayobami Elisha Oseyemi et al 2022 J. Electrochem. Soc. 169 126501 DOI 10.1149/1945-7111/aca129

1945-7111/169/12/126501

Abstract

Microphotosynthetic Power Cells (μPSCs) have emerged as a promising bioelectricity generation technology with the potential to meet the low-power application demand in a sustainable, and environmentally friendly manner by leveraging the photosynthetic capabilities of autotrophs. Internal losses connected to the transfer of charges from the photosynthetic organisms to the electron acceptor (anode electrode), however, continue to pose a serious challenge to the efficiency of the system. Over the years, many different designs have been reported. The potential of boosting power density with device miniaturization is discussed in this study as it provides a crucial pathway for performance enhancement.

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Photosynthesis, the world's oldest energy conversion process, relies on light energy and water, the most abundant resources available, to keep green life going. 1,2 During photosynthesis, CO2 is reduced into chemical energy to fuel cellular activities, giving off oxygen as a byproduct. 3 Biological electrochemical systems (BECs), like the Microbial Fuel Cell (MFC) 46 and the μPSC 79 (also referred to as biophotovoltaic cell (BVC), 10 microphotosynthetic electrochemical cell (μPEC), 11 and microfluidic bio-solar panel 12 in the literature) have emerged a promising alternative to fossil combustibles to meet the rising global energy demand. The μPSC is characterized by its use of living organisms, precisely oxygenic photosynthetic organisms, as "natural" solar panels - cheap, self-regenerating, and readily available - for electricity generation; unlike its counterpart which uses heterotrophic bacteria as biocatalysts - to catalyze the oxidation of organic substrates (e.g., biomass, waste-water, etc.). Currently, the conversion efficiency of the latter is higher, 13,14 but the organic fuels it relies on are not inexhaustible, as opposed to the former's energy source—the Sun—which is near-infinite and widely available. μPSCs are currently unable to convert the photosynthetic microorganisms' high energy conversion efficiency into power output. 15 As a result, extensive research from both biological and engineering perspectives is required to determine what the limiting factors are. The working principles of the μPSC and the MFC are illustrated in Figs. 1a and 1b respectively.

Figure 1.

Figure 1. Schematic describing the operating principle of (a) a Microphotosynthetic power cell (μPSC), and (b) a microbial fuel cell (MFC). (c) i A descriptive 3D model of the μPSC, ii Top view showing the anode work area. The fabrication process is described in Ref. 16.

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The BECs have over the years transitioned through a series of model changes geared toward performance enhancement. The more established MFCs 13,1722 have received a lot of attention and have played an important role in the optimization of the rather nascent μPSC. 2,7,12,23,24 Miniaturization in a general sense offers huge potential for improved precision and throughput in cell studies. It has found huge usefulness in microfluidic cell studies, which allows for small culture volume, as well as single-cell studies—useful in identifying salient genetical characteristics which could, in turn, be used to direct the development of certain efficient cell lines, 2527 in bioelement detection, 2729 cell separation, 30 and so on. Similarly, in the context of bioelectricity generation with PSCs, miniaturization reduces the distance charges released by the donors (photosynthetic organisms) have to travel to reach the acceptor (the anode electrode), minimizing resistive losses in the anolyte. 4

Working of The μPSC

The typical architecture and working of the μPSC are described in Fig. 1a. It comprises two chambers, an anode chamber—containing the anode electrode and the photosynthetic microorganisms (e.g., algae, cyanobacteria, etc.), and a cathode chamber, comprising the cathode electrode. Both chambers are separated by a unit comprising a proton exchange membrane (PEM) sandwiched by the anode and cathode electrode, often referred to as membrane electrode assembly (MEA). Electron transfer from the microbes to the anode electrode can be through direct cell contact (cytochrome based), 31,32 direct nanowire contacts, 33 or mediator supported. 8,16 The electron travels from the anodic electrode via an external circuit (as seen illustrated in the figure) to produce electricity as they continue to the cathode. The protons, on the other hand, transit through the PEM (commonly made of Nafion - sulfonated tetrafluoroethylene-based fluoropolymer) to the Cathode compartment. The PEM at the same time prevents the cross-flow of the electrons. The cathodic reaction is often a function of the type of electron acceptor used; 8,34,35 nevertheless, in all, the diffused protons recombine with oxygen in the cathode section (i.e. the electron donor is re-oxidized, and oxygen gets reduced) to produce water, carbon dioxide, and energy. The chemical equation of photosynthesis and respiration are as follows:

Photosynthesis:

Light-dependent

Respiration

Light-independent

Algae have been used extensively in the μPSCs for their characteristic photosynthetic nature, and more so, for their ability to grow fast and as well survive adverse weather conditions. Species like Chlamydomonas reinhardtii, Dunaliella tertioelecta, and Chlorella vulgaris have garnered the most attention, according to the literature. 8,16,34

Applicability

The μPSC is applicable in various ultra-low and low-power (0.1–100 mW) applications. For instance, in a very recent study, a single unit of the μPSC was shown capable of powering a microprocessor (Arm Cortex M0+) for six months. 36 There is another study that showed its utility in an internet of things (IoT) humidity sensor (0.18 mV), 37 explorable in remote weather monitoring. The μPSC can also be used to power IoT sensors in autonomous vehicles, and ultrasonic sensors, given their low power requirements (0.2–80 mW). 3739 More so, a combination of two or more PSC devices in parallel or series arrays could be used to meet higher power demands. For further details on the application potentials of the μPSC technology, readers can refer to our previous works. 9,40

Current status

While still in its early stages, the μPSC holds a lot of potential for a carbon-negative power supply. Based on the literature, the μ-PSC designs can produce open-circuit voltages in the range of 100–993 mV and short circuit currents in hundreds of μA, current densities in the range of 0.2–3000 mA m−2, and power densities ranging from 0.0004 to 715 mW m−2. 8,16,23,34,4143 Thus far, the maximum power reported of a single μPSC device reported is 715 mW m−2, 42 which involved the use of gold nanoparticles in the anode chamber to enhance photon absorption as well as electron transport from the microorganism (algae - Chlamydomonas reinhardtii) to the anode surface. Although this represents a significant advancement for micro-biological solar cells generally, considerable work remains to be done to fulfill commercial requirements. For more information on the development of the μPSC technology, readers are referred to Refs. 4, 8, 4245.

Performance measurement

Some common parameters for quantifying the performance of the μPSC include, open-circuit voltage (OCV), current density (CD), power (P), power density (PD), polarization and power curves, quantum yield, and Coulombic efficiency, ${\varepsilon }_{C}.$ 5,24 The OCV quantifies is the maximum potential obtainable from the cell, measured from the terminals of the cell in the absence of an external load or electric current - as opposed to the maximum potential attainable in the cell (i.e., the ideal voltage). The ideal voltage (~1.2 V in an air-cathode MFC: 0.805 V from the cathode and −0.42 V from the anode 5 ), which corresponds to the cell emf (${V}_{emf}$)/Nernst reversible voltage (NRV), comes in the absence of internal losses (such as ohmic, concentration and activation losses). The current divided by the total electrode area gives the CD. It reflects the inherent rates of charge transfer between analytes and the electrode, providing insights into the structure and interrelation of the analyte and the current collector. Measured cell voltage ${V}_{cell}$ is often a linear function of the current, and simply described as $OCV\,=\,{V}_{cell}\,-\,I{R}_{int},$ where $I{R}_{int}$ is the summation of all internal losses of the μ-PSC, proportional to the system's internal resistance ${R}_{int}$ and generated current $I.$ Power is estimated $I{V}_{cell};$ the voltage is taken across a fixed external resistor ${R}_{ext},$ while the current $I$ is estimated from ${V}_{cell}/{R}_{ext}.$ Hence, power is estimated normally as ${V}_{cell}^{2}/{R}_{ext}.$ The PD is useful for comparing the power yield of different systems. Power is normalized to a characteristic feature of the generating system, usually the effective anode surface area, as it is where the biological reactions take place. 4,8,45 Further discussions on the PD will be presented in the next section. The Coulombic efficiency basically describes the efficiency of the system in harnessing electrons from the photosynthetic organisms; in terms of the ratio of electrons recovered to the amount available in the system if all the microorganisms produced current. 46

Power density, a key factor for performance comparison and optimization

The PD is basically a measure of the power generated by a device divided by the size of the device. At the macrolevel, it presents a straightforward approach to compare any power product towards efficiency enhancement as well as for thermal considerations. In the BES settings, it quantifies the performance in terms of power output per electrode size (active surface area, in particular), with a common unit of measurement of PD in milliwatts per meter square (mA/m2). Hence, one simple approach to increasing PD is reducing component size (that is, miniaturization). It principally provides the benefit of higher surface-to-volume ratio, hence, heat—a critical efficiency parameter of any electrical/mechanical system—is dissipated faster than stored; and a system that releases energy quickly can also recharge quickly. In addition to this, there is also the advantage of component integration. Energy supply from components small enough to fit inside a cell phone or camera flash, for instance, and sufficient to power the device makes an ideal high-power density system. Similarly, in BECs, in addition to the benefits of reduced anolyte volume and shorter charge transport length scales, the thermal performance of the system is enhanced by the dominance of heat dissipation over heat storage, resulting in greater efficiency, measurable through the PD. This is highlighted by our assessment of the several types of PSC designs that have been reported during the past two decades, which is summarized in Fig. 2. For ease of classification and a fair comparative basis, devices that implemented external performance boosters like gold or silver nanoparticles, as in Refs. 42, 47, and the like are left out.

Figure 2.

Figure 2. The trend of Power Density increase with decreasing component size in the last two decades (Details in Appendix).

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As earlier indicated, the main goal of this work is to examine the relationship between size reduction and power output from the several different uPSC designs that have been reported during the past two decades. In essence, miniaturization enhances the physical proximity of the biocatalyst organisms to the anode surface, shortening the length scale of charge transfer and reducing resistive loss in the electrolyte as a result. By contrast, in macro BECs, where charges must travel longer distances, factors including ohmic polarization, reaction kinetics, and concentration (mass transport) polarization are known to have significant limiting impacts on power outputs. 4,22

Figure 2 presents an overview of the Power Densities of intrinsic μPSCs (that is, with no external energy booster) from recent literature data (details in supplementary Table A). While other factors such as biocatalyst agents' photosynthetic capacity, electrode material, light intensity and so on all play a role in the device's electrical output, increasing the surface-to-volume ratio of the working unit through miniaturization offers great prospects for optimizing the overall performance of the μPSC technology. There are also instances where extrinsic energy inputs have been used to obtain significant power density boosts. 42,43,48 Nevertheless, a comprehensive review of the literature, summarized in Fig. 2, reveals a noteworthy connection between miniaturization (measured in terms of anode surface area) and gains in power density. Clearly, most of the reported works have shown lower power density with higher anode area (highlighted by the rectangular box in the figure). The green ellipse, on the other hand, demonstrates the higher power densities amongst all the listed μPSCs. The studies, in other words, demonstrated relatively optimum anode surface areas. This in all emphasizes the need for optimal anode area design in order to increase the PSC's power density.

Subsequently, to push the μPSC technology to levels suitable for real-world applications, two or more units of the μPSC device can be arrayed in diverse configurations to obtain an optimized total operating voltage and current, sufficient to meet the demands of low-power devices. 49 The various array configurations and their power output have been investigated and it was suggested to design the array configurations based on the power requirement. To this end, the beauty of miniaturization, which offers a huge promise of power enhancement through optimal work area design and the combining of many small units, becomes even more tangible in our quest to push green energy to the greatest heights.

Challenges and Future Needs

Even though the μPSC technology is capable of producing power in both light and dark conditions, quite a few intrinsic and extrinsic limiting factors still abound, posing an impediment to its commercial application. Efforts and investment are, however, increasingly on the rise towards resolving these issues and achieving reliable operational cost-effective performance. 10,16,42,5052 The various issues relating to design, fabrication complexity, manufacturing cost, modeling, materials, and operating conditions are described in our prior study. 9 We have also, in another study, discussed the enormous application potential of the technology, in the effort to reduce our dependence on fossil combustibles which continually pose a threat to our ecosystem. 40 Although the idea of improving power density by lowering component sizes is very practical , there is a limit to the strategy because size is also a key factor in the actual component value. As a result, more research is needed to establish the limits and bounds of miniaturization, as well as component arrays (how small is too small, and how large of an array would be most efficient) -from the perspective of overall system efficiency, and to establish a guide for making informed tradeoffs toward relevant design optimization.

Summary

The eco-friendly μPSC technology thus far is capable of power densities just in 100 s of ${\rm{mW}}/{{\rm{m}}}^{2}.$ A way to improve power output is by increasing interaction between the electron-donating photosynthetic organisms and the electron-accepting electrode through miniaturization. As power density becomes a more important factor in comparing power products (dc-dc converters, power amplifiers, etc.), power circuit design and supply, and others, future μPSC studies need to closely look at minimizing internal losses, enhancing thermal performance, as well as increasing integration for efficient sustainable performance in commercial applications.

Acknowledgments

The authors acknowledge the financial support of M.P. from the Natural Sciences and Engineering Research Council of Canada (NSERC), New Frontiers Research Fund, and Concordia Research Chair.

Appendix

Table A·I.

Table A·I. List of photosynthetic power cell studies in recent years (in the order of increasing anodic electrode area).

Study (First Author, Date)Device nameActive Anode Area [mm2]Active Anode Volume [μl]Power Density [mW m−2]Mechanism for electron export (Anode)Photosynthetic organism
Bombelli, 2014 10 Bio-photovoltaics0.030.4105FreeSynechocystis sp. PCC 6803
Saar, 2018 50 Bio-voltaic device0.081000300K3[Fe (CN)6]Synechocystis sp. PCC6803 cells
Saar, 2018 50 Bio-voltiac device0.081000500K3[Fe (CN)6]Synechocystis sp. PCC6803 -mutant cells
Torabi, 2021 53 Biophotovoltaics0.91.8 × 106 220.7FreeThermosynechococcus elongatus BP-1
Mohammadifar, 2020 54 Bio solar cell1.21056.4FreeSynechocystis sp. PCC6803
Sekar, 2014 55 Photo-bioelectrochemical cells2.5n/a1001,4-benzoquinoneNostoc sp.
Masi, 2020 56 Biofuel cell1350340FreeThykalod membranes of Spnach plants
Yoon, 2014 57 Microbial Solar Sell28570.0709 Cyanobacteria, Synechocystis, PCC 6803
Liu, 2017 58 Micro biological solar cell38.590438FreeSynechocystis sp. PCC 6803
Chiao, 2006 17 Photosynthetic electrochemical cell (μPEC)504.30.0004MethyleneBlue Anabaena sp.
Liu, 2019 59 Biological solar cell50.3100107FreeSynechocystis sp. PCC6803, Shewanella oneidensis MR-1
Bombelli, 2011 7 Bio-photovoltaics8015010.2[Fe (CN)]3− Synechocystis sp. PCC 6803
Senthiljumar, 2018 60 Biophotovoltaics100100000.036FreeChlorella vulgaris
Thong, 2021 61 Biophotovoltaics200n/a0.04FreeChlorella vulgaris
Shahparnia, 2015 8 Photosynthetic power cell2202000362.2Methylene Bluechlamydomonas reinhardtii
Ramanan, 2015 16 Photosynthetic power cell2202000400Methylene Bluechlamydomonas reinhardtii
Thorne, 2011 62 Photo-microbial fuel cell230230024[Fe (CN)]3− Chlorella vulgaris
Saper, 2018 63 Bio-electrophotochemical cell2545200.4FreeSynechocystis sp. PCC6803 cells
Schneider, 2016 64 Photo- microbial cell fuel390310014.5Fe (CN)3− C. vulgaris
Inglesby, 2013 65 Photosynthetic microbial fuel cell40040000.0248FreeMixed photosynthetic biofil consortia
Firoozabadi, 2021 66 Biophotovoltaics400880148.27FreeSynechocystis sp. PCC6803
Cevik, 2020 67 Bio-electrochemical fuel cell625n/a42.2FreeGreen alga Choricystis sp.
Zhu, 2019 68 Bio-photovoltaic cell6251.4 × 105 150FreeSynechococcus elongatus UTEX 2973
Gonzalez, 2015 69 Photosynthetic microbial fuel cell8008 × 105 42.98 Activated sludge
Bombelli, 2022 36 Aluminium Biophotovoltaic System8601440042FreeSynechocystis sp. PCC 6803
Bombelli, 2022 36 Aluminium Biophotovoltaic System1020n/a0.4FreeSynechocystis sp. PCC 6803
Siu, 2008 19 Photosynthetic Electrochemical cell120015.60.0004Methylene BlueAnabaena sp. (Suspension)
Ng, 2014 70 Bio-photovoltaics1225n/a0.27FreeChlorella sp. (UMACC313)
Ng, 2018 71 Bio-photovoltaic cell12255 × 105 0.32FreeSynechococcus elongatus (UMACC 105)
Ng, 2018 71 Bio-photovoltaic cell12255 × 105 0.538FreeSynechococcus elongatus (UMACC 105)
Sawa, 2017 72 Biophotovoltaics1250n/a0.38FreeChlorella sp. UMACC 313
Gouveia, 2014 73 Photosynthetic alga microbial fuel cell12605000062.7 Bacterial Consortium
McCormick, 2011 15 Bio-photovoltaic cell13001260010FreeSynechococcus sp. WH 5701
Bradley, 2013 74 Bio-photovoltaic cell1300315000.2FreeSynechocystis TM
Luimstra, 2014 75 Photosynthetic microbial fuel cell1400700006FreePauschulzia pseudovolvox
Madiraju, 2012 76 Microbial fuel cell1500600000.3FreeSynechocystis sp. PCC 6803
Wu, 2014 77 Photo-microbial fuel cell16001.25 × 105 64.2FreeDesmodesmussp. A8
Bombelli, 2012 78 Bio-photovoltaics2000200000.02FreeOscillatoria limnetica
Nishio, 2010 79 Photo-bioreactor2000n/a3.2FreeGreen hot spring microbial mat (Biofilm)
Gunaseelan, 2021 80 Biophotovoltaics200080000275FreeEffective Mirobes(EM) and Anaeroubic sludge bank reactor (UASB)
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10.1149/1945-7111/aca129