Research article Special Issues

Bioelectricity production from anaerobically treated leachate in microbial fuel cell using Delftia acidovorans spp.

  • Received: 19 November 2023 Revised: 01 December 2023 Accepted: 06 December 2023 Published: 18 December 2023
  • Microbial fuel cells (MFCs) are devices that use microorganisms to produce electricity from organic matter. In this study, the bacterium Delftia acidovorans spp was used to evaluate energy generation in a single-chamber MFC. In this evaluation, six MFCs were assembled with different exchange membranes: two with carbon fiber composite membrane, two with maghemite membrane and two with heat-treated maghemite. Synthetic maghemite was characterized using X-ray powder diffraction (XRD), X-ray photoelectron spectroscopy (XPS), Brunauer-Emmett-Teller (BET) and Fourier transform infrared spectroscopy (FTIR) measurements. Bioelectricity monitoring in the MFCs was conducted for 15 days, with data collected every 60 seconds. The cell that achieved the highest bioelectricity production was the one with heat-treated maghemite, reaching a production of 286.50mV. It used 100% leachate from fruit and vegetable waste as a substrate, starting with values of 365 mg/L of N-NH4, 96000 mg/L of biochemical oxygen demand (BOD5), 101500 mg/L of chemical oxygen demand (COD) and a pH of 4.11. In the results, the carbon fiber treatment had a higher removal efficiency percentage of up to 63.38% for BOD5 and 69.67% for COD. For ammonium nitrogen removal, all cells showed good removal efficiency of up to 92.49%. The pH value increased in all treatments due to the degradation of organic matter, reaching a value of up to 5.96. Thus, the efficiency of Delftia acidovorans spp. and carbon fiber are a good alternative as an exchange membrane in purifying leachate contaminants within an MFC.

    Citation: Cristina Calderón-Tapia, Daniel Chuquín-Vasco, Alex Guambo-Galarza, Soledad Núñez-Moreno, Cristina Silva-Cisneros. Bioelectricity production from anaerobically treated leachate in microbial fuel cell using Delftia acidovorans spp.[J]. AIMS Environmental Science, 2023, 10(6): 847-867. doi: 10.3934/environsci.2023046

    Related Papers:

    [1] Okechukwu Okafor, Abimbola Popoola, Olawale Popoola, Samson Adeosun . Surface modification of carbon nanotubes and their nanocomposites for fuel cell applications: A review. AIMS Materials Science, 2024, 11(2): 369-414. doi: 10.3934/matersci.2024020
    [2] Christoph Nick, Helmut F. Schlaak, Christiane Thielemann . Simulation and Measurement of Neuroelectrodes Characteristics with Integrated High Aspect Ratio Nano Structures. AIMS Materials Science, 2015, 2(3): 189-202. doi: 10.3934/matersci.2015.3.189
    [3] Falko Böttger-Hiller, Klaus Nestler, Henning Zeidler, Gunther Glowa, Thomas Lampke . Plasma electrolytic polishing of metalized carbon fibers. AIMS Materials Science, 2016, 3(1): 260-269. doi: 10.3934/matersci.2016.1.260
    [4] Christian M Julien, Alain Mauger, Ashraf E Abdel-Ghany, Ahmed M Hashem, Karim Zaghib . Smart materials for energy storage in Li-ion batteries. AIMS Materials Science, 2016, 3(1): 137-148. doi: 10.3934/matersci.2016.1.137
    [5] Nagesh K. Tripathi . Porous carbon spheres: Recent developments and applications. AIMS Materials Science, 2018, 5(5): 1016-1052. doi: 10.3934/matersci.2018.5.1016
    [6] Claas Hüter, Shuo Fu, Martin Finsterbusch, Egbert Figgemeier, Luke Wells, Robert Spatschek . Electrode–electrolyte interface stability in solid state electrolyte systems: influence of coating thickness under varying residual stresses. AIMS Materials Science, 2017, 4(4): 867-877. doi: 10.3934/matersci.2017.4.867
    [7] Jamal Alnofiay, Ahmed Al-Shahrie, Elsayed Shalaan . Green synthesis of high-performance gallium oxide supercapacitor: A path to outstanding energy density. AIMS Materials Science, 2024, 11(6): 1065-1082. doi: 10.3934/matersci.2024051
    [8] Christoph Janiak . Inorganic materials synthesis in ionic liquids. AIMS Materials Science, 2014, 1(1): 41-44. doi: 10.3934/matersci.2014.1.41
    [9] Giovanna Di Pasquale, Salvatore Graziani, Chiara Gugliuzzo, Antonino Pollicino . Ionic polymer-metal composites (IPMCs) and ionic polymer-polymer composites (IP2Cs): Effects of electrode on mechanical, thermal and electromechanical behaviour. AIMS Materials Science, 2017, 4(5): 1062-1077. doi: 10.3934/matersci.2017.5.1062
    [10] Christian M. Julien, Alain Mauger . Functional behavior of AlF3 coatings for high-performance cathode materials for lithium-ion batteries. AIMS Materials Science, 2019, 6(3): 406-440. doi: 10.3934/matersci.2019.3.406
  • Microbial fuel cells (MFCs) are devices that use microorganisms to produce electricity from organic matter. In this study, the bacterium Delftia acidovorans spp was used to evaluate energy generation in a single-chamber MFC. In this evaluation, six MFCs were assembled with different exchange membranes: two with carbon fiber composite membrane, two with maghemite membrane and two with heat-treated maghemite. Synthetic maghemite was characterized using X-ray powder diffraction (XRD), X-ray photoelectron spectroscopy (XPS), Brunauer-Emmett-Teller (BET) and Fourier transform infrared spectroscopy (FTIR) measurements. Bioelectricity monitoring in the MFCs was conducted for 15 days, with data collected every 60 seconds. The cell that achieved the highest bioelectricity production was the one with heat-treated maghemite, reaching a production of 286.50mV. It used 100% leachate from fruit and vegetable waste as a substrate, starting with values of 365 mg/L of N-NH4, 96000 mg/L of biochemical oxygen demand (BOD5), 101500 mg/L of chemical oxygen demand (COD) and a pH of 4.11. In the results, the carbon fiber treatment had a higher removal efficiency percentage of up to 63.38% for BOD5 and 69.67% for COD. For ammonium nitrogen removal, all cells showed good removal efficiency of up to 92.49%. The pH value increased in all treatments due to the degradation of organic matter, reaching a value of up to 5.96. Thus, the efficiency of Delftia acidovorans spp. and carbon fiber are a good alternative as an exchange membrane in purifying leachate contaminants within an MFC.



    1. Introduction

    An increasing reliance on portable electronics has motivated the recent investigation of wearable energy storage systems. Viable energy storage solutions for wearable applications should be safe for the consumer, lightweight, physically flexible, and straightforward to manufacture. Use of a solid-state gel electrolyte may enable a fully printable device architecture that can satisfy all of these requirements [1]. Ionic liquid-based gels, or ionogels, offer an attractive way to realize a safe supercapacitor electrolyte due to the negligible vapor pressure of the ionic liquid, which renders it nonvolatile and nonflammable.

    Ionogels are composite materials that consist of an ionic liquid and a solid support matrix of organic, inorganic, or hybrid composition. The matrix can be formed by physical coagulation of a solid additive (e.g. carbon nanotubes, fumed silica, organic gelators), or through chemical reaction [2]. Electrolyte gels that employ a polymer-based matrix have widely been used to demonstrate flexible supercapacitor prototypes due to their physical integrity [3, 4]. It has recently been shown that ionogels formed in situ by UV-initiated free radical polymerization are extremely simple to fabricate, and possess desirable characteristics as solid electrolytes [5, 6]. However, few studies have explored the integration of UV-cured ionogel electrolytes with carbon electrodes due to the inherent difficulty of irradiating a thin film of gel precursor solution s and wiched between opaque carbon electrodes with UV light [7].

    Solid-state, flexible supercapacitor prototype assembly can be broadly classified into two categories: (1) a multi-step approach, whereby the surfaces of two distinct carbon electrodes are first coated with a gel electrolyte and subsequently s and wiched together [8, 9, 10, 11, 12], or (2) a one-step approach, whereby a gel electrolyte is formed in situ against two carbon electrodes that have already been arranged in their desired final geometry within the device [13, 14]. Although the multi-step process is feasible in a laboratory setting, a one-step process would provide a simpler approach to both scale-up and large-scale production. Furthermore, by eliminating the need to mechanically press two halves of the device together, one-step assembly greatly reduces the possibility of damaging the typically fragile high surface area carbon electrodes employed in supercapacitors. With several groups currently developing novel types of high surface area carbon-based electrodes [15, 16, 17, 18, 19], there is a critical need to underst and how ionogel electrolytes can be effectively combined with these structures in situ.

    The work described here examines the integration of an in situ UV-cured poly (ethylene glycol) diacrylate (PEGDA) -supported ionogel electrolyte [6] with several commercially available, high surface area carbon paper electrodes. In order to cure the gel electrolyte in situ adjacent to both carbon electrodes, a coplanar test bed architecture was employed. This approach served as a repeatable means of forming a thin UV-cured ionogel film in contact with different pairs of opaque carbon electrodes in a single step. In addition, a direct comparison of the electrical response of the ionogel electrolyte with that of the neat ionic liquid, 1-ethyl-3-methylimidazolium bis (trifluoromethylsulfonyl) imide (EMI TFSI), was performed in order to examine the hypothesis that the performance of a particular carbon electrode with neat EMI TFSI is directly correlated to its performance with the PEGDA-supported ionogel electrolyte.

    2. Materials and Method

    2.1. Coplanar Test Bed Assembly

    Ionogel-carbon paper electrode assemblies were fabricated with a coplanar electrode geometry on glass microscope slides. PTFE pipe thread tape was used to define a rectangular area of 60 mm2 (12 mm x 5 mm), inside which the active components of the device were located. A portion of each carbon paper was initially immersed in melted paraffin wax (McMaster Carr). After this treatment, the carbon paper was cut such that an uncoated carbon paper projected area of 25 mm2 (5 mm x 5 mm) was exposed directly adjacent to the edge of the paper treated by the paraffin wax. This area represents the active part of each electrode that was wetted by electrolyte. Two electrodes were cut out in this fashion and placed flat on the glass slide within the area bordered by the PTFE tape. A gap of 2 mm was maintained between the edges of the carbon paper electrodes for all assemblies. An electrolyte solution volume of 30 µL (either neat ionic liquid or the ionogel precursor solution, see below) was pipetted into the PTFE-bounded region containing the carbon electrodes from above. Electrical contact was made using nickel-plated steel micro-alligator clips that gripped the paraffin-treated portion of the carbon papers against the glass slide. Ionogel devices were assembled and tested in a nitrogen-filled glovebox (< 1 ppm oxygen and water vapor). Devices made with the neat ionic liquid were assembled and tested under ambient laboratory conditions.

    2.2. High Surface Area Carbon Papers and the Ionogel Electrolyte

    High surface area carbon papers were procured from three sources. Graphitized carbon fiber paper (CFP), manufactured by Engineered Fibers Technology, was obtained from an online materials supplier. Carbon aerogel paper (CAGP) was manufactured by and obtained from Marketech International. Carbon nanotube paper (CNTP) was manufactured by and obtained from Inorganic Specialists, Inc.; four different variations of this paper were examined (CNTP1, CNTP2, CNTP3, and CNTP4). The sheet resistances of all carbon papers were measured using a four-point probe instrument (Creative Design Engineering). The manufacturer-reported specific surface areas and the measured sheet resistance values of each carbon paper are summarized in Table 1.

    Table 1. Properties of high surface area carbon paper electrodes.
    Carbon Electrode Reported Specific Surface Area (m2 g-1) Measured Sheet Resistance (Ohm sq.-1) Binder Present?
    CFP 80 0.5 yes
    CAGP 600 1.3 no
    CNTP1 60 5.1 no
    CNTP2 180 5.0 no
    CNTP3 220 14.7 no
    CNTP4 400 3.4 no
     | Show Table
    DownLoad: CSV

    The solid ionogel electrolyte was fabricated following the method of Visentin and Panzer [6]. The ionic liquid, 1-ethyl-3-methylimidazolium bis (trifluoromethylsulfonyl) imide (EMI TFSI), was obtained from EMD Chemicals. The polymer scaffold precursor, polyethylene glycol diacrylate (PEGDA), and UV-initiator, 2-hydroxy-2-methylpropiophenone, were obtained from Sigma Aldrich. A polymer content of 16% wt. PEGDA was selected based on its ease of h and ling and flexible character [6]. After dispensing the ionogel precursor solution on top of the coplanar electrode assembly, UV irradiation for 3 min (from the top) was used to create the gel electrolyte. All chemicals used to create the ionogel electrolyte were stored and used in the nitrogen-filled glovebox.

    Cyclic voltammetry (CV) and electrical impedance spectroscopy (EIS) were performed using a potentiostat with a built-in frequency response analyzer (VersaSTAT 3, Princeton Applied Research). CV was conducted at a voltage sweep rate of 1 mV s-1 within a window of -1.5 V to +1.5 V (vs. open circuit); at least three cycles were recorded to ensure repeatability between successive voltage sweeps. For each EIS measurement, the frequency was logarithmically swept from 10 kHz to 1 mHz. The RMS amplitude of the AC signal employed was 10 mV (DC offset of 0 V vs. open circuit).

    3. Results and Discussion

    3.1. Carbon Paper Electrodes

    Scanning electron microscopy (SEM) was used to examine the microstructure of the various carbon papers employed in this study. Figure 1 shows representative SEM images obtained for the carbon fiber paper (CFP), carbon aerogel paper (CAGP), and carbon nanotube paper #3 (CNTP3); it should be noted that the four CNTP papers (CNTP1-4) all appeared visually similar when viewed under 5000 x magnification.

    Figure 1. SEM images of the three main carbon paper types employed: (a) carbon fiber paper (CFP); (b) carbon aerogel paper (CAGP); (c) carbon nanotube paper #3 (CNTP3), which is representative of all four CNTP materials used in this study. Insets to (b) and (c) show the pore structures of these papers at higher magnification..

    CFP is a porous carbon paper that is typically used for laboratory scale fuel cell development. It consists of a graphitized network of resin-bonded carbon fibers, and , as seen in Figure 1a, CFP exhibits the largest apparent pore size among all of the papers utilized in this study. It is important to note that the CFP material was the only electrode studied that contained a binder for physical support (Figure 1a).

    According to its manufacturer (Marketech International, Inc.), the CAGP material is prepared by a sol-gel method from a resorcinol-formaldehyde precursor, which, post-reaction, is carbonized to create a carbon foam with high porosity and surface area. To create a robust paper electrode, the CAGP also contains carbon fibers for mechanical support (Figure 1b). Inside the micron-scale cracks present on the surface of the CAGP electrodes, the nanoporous carbon foam structure is visible (pore size of approximately 80 nm, see inset to Figure 1b), which gives the CAGP material its very high reported specific surface area of 600 m2 g-1.

    Four types of carbon nanotube paper were obtained from Inorganic Specialists, Inc. (CNTP1-4). All of the CNTP materials consist of 100% carbon nanotubes/fibers, with no binder present (Figure 1c). Such papers are fabricated by dispersing carbon nanotubes/fibers in water, thenfiltering the suspension through a porous support membrane to produce a carbon filter cake [20]. Due to the absence of any binder material, the CNTP electrodes were the most fragile to h and le. Variation in the reported specific surface areas of the four CNTP materials utilized in this study was likely achieved by the manufacturer incorporating carbon nanotubes of different diameters and /or lengths, as evidenced by SEM imaging at high magnification (inset to Figure 1c).

    3.2. Cyclic voltammetry

    Figure 2 displays the CV curves obtained for coplanar test beds fabricated with the six different types of carbon paper electrodes examined and the ionogel electrolyte; current values are normalized by the total mass of two electrodes. Each curve exhibits an approximately rectangular shape, indicating that capacitive behavior was observed for all of the carbon papers. If it is assumed to be independent of voltage, the capacitance of each device can be calculated directly from the current values measured during the CV sweeps via:

    C=1dVdt

    Figure 2. Cyclic voltammograms of test beds containing different carbon paper electrodes with 16 wt% PEGDA ionogel electrolyte (third cycle shown in each case). A scan rate of 1 mV s-1 was used.

    The positive current value measured at 0 V on the CV graph was used to calculate the capacitance of each device (the absolute values of the negative currents were nearly identical to the positive current values). Gravimetric capacitances for each electrode type integrated with the ionogel electrolyte are summarized in Table 2. The capacitance values can be approximately correlated with the reported surface areas of the carbon papers (shown in Table 1), with one notable exception; namely, the capacitance of the CFP device (0.02 F g-1) was nearly two orders of magnitude lower than was observed for the other electrode papers. Although its reported specific surface area was relatively low (80 m2 g-1), the CFP material exhibited significantly lower capacitance compared to the CNTP1 material, which claimed a similar specific surface area of 60 m2 g-1. This discrepancy is likely due to the presence of the binder in CFP (Figure 1a), which reduces either the wettability of the electrode by the ionogel precursor solution, and /or the effective (conductive) electrode surface area.

    3.3. Electrical Impedance Spectroscopy

    Figure 3 displays Bode plots of the phase angle of impedance (φ) obtained for each carbon paper type, together with the neat EMI TFSI ionic liquid (Figure 3a) or the ionogel electrolyte (Figure 3b). The frequency at which the phase angle reaches -45° (f0) is termed the “switching frequency, ” where a device transitions from exhibiting primarily resistive to primarily capacitive behavior. Comparison of the neat EMI TFSI and ionogel electrolytes shown in Figure 3 reveals that the neat EMI TFSI devices uniformly exhibited switching frequencies approximately five times faster than their ionogel counterparts. This difference is due to the presence of the cross-linked PEGDA scaffold in the ionogel, which impedes the polarization response of the ions [6]. The switching frequency for CFP with the ionogel electrolyte (f0 = 6.3 Hz) was observed to be approximately three orders of magnitude larger than for the other carbon papers examined (f0 varies between 2-10 mHz), as seen in Figure 3b. It should be pointed out that these values are lower than those typically reported for supercapacitor prototypes, due to the coplanar electrode architecture employed here. However, a comparison of the EIS behavior of the various carbon paper electrodes for a given electrolyte (either neat ionic liquid or the ionogel) can illuminate differences in the relative performance of each carbon structure. The comparatively fast switching frequency observed for CFP with both electrolyte types is attributed to the large, open pore structure defined by the carbon fibers of this material (Figure 1a), which facilitates ready access to the EMI and TFSI ions for rapid double layer formation and rearrangement. However, the low effective surface area of the CFP material that enables a fast polarization response also leads to the lowest observed capacitance (Figure 2).

    Figure 3. Bode plots of the phase angle of impedance for test beds containing: (a) neat EMI TFSI electrolyte; (b) 16 wt% PEGDA ionogel electrolyte.





    The magnitude of impedance (|Z|) versus frequency data measured using the neat ionic liquid and ionogel electrolyte test beds are shown in Figure 4. While it is noted that the equivalent series resistance (ESR) values obtained here are much larger than those of typical supercapacitor devices (due to the coplanar structure of the test bed), relative comparisons among the carbon papers are highly informative. The CAGP and CFP materials exhibited lower ESR values (taken to be equal to |Z| at f = 10 kHz) compared to the other electrode materials with both neat EMI TFSI (Figure 4a) as well as with the ionogel electrolyte (Figure 4b), as summarized in Table 2. This result was expected since these two electrode materials possessed the lowest measured sheet resistances (Table 1). However, a different trend is observed within the group of CNTP materials upon comparing their behavior with the neat ionic liquid versus the ionogel electrolyte. The order of carbon nanotube paper sheet resistances, from highest to lowest, is: CNTP3 > CNTP1 ≈ CNTP2 > CNTP4 (Table 1). This trend is mirrored in the ordering of device ESR values when EMI TFSI is used as an electrolyte (Figure 4a), but is not the case when the ionogel electrolyte is employed (Figure 4b). As seen in Table 2, the ESR value of the CNTP3 device with the ionogel electrolyte (9.74 kw) is, in fact, lower than those for both the CNTP1 and CNPT2 devices (11.7 kw and 10.2 kw respectively). Furthermore, CNTP4, which exhibited the lowest measured sheet resistance among the four carbon nanotube-based papers and demonstrated a low ESR value when paired with the neat ionic liquid (0.615 kw), displayed an unexpectedly large relative increase in ESR when integrated with the solid ionogel electrolyte (6.98 kw). As shown in Table 2, the relative increase in ESR between the ionogel and the neat EMI TFSI responses ranged from 3.9x (for CNTP3) to as large as 11.3x (for CNTP4).

    Figure 4. Magnitude of impedance, |Z|, for test beds containing: (a) neat EMI TFSI electrolyte; (b) 16 wt% PEGDA ionogel electrolyte.
    Table 2. Performance of test bed devices with 16 wt% PEGDA ionogel.
    Carbon Electrode Specific Capacitance (F gelectrodes-1) Equiv. Series Resistance (kw) ESRionogel/ESREMI TFSI (-)
    CFP 0.02 3.88 6.1
    CAGP 2.33 2.25 4.3
    CNTP1 0.97 11.7 9.8
    CNTP2 1.63 10.2 7.0
    CNTP3 1.30 9.74 3.9
    CNTP4 1.87 6.98 11.3
     | Show Table
    DownLoad: CSV

    Since identical electrolyte solutions and fabrication conditions were employed for each carbon paper electrode test bed, one may attribute differences in performance of the various electrode materials when changing from the ionic liquid to the ionogel electrolyte to differences in wettability and /or interfacial compatibility. More specifically, the formation of the cross-linked PEGDA scaffold inside the ionic liquid during UV-curing of the ionogel precursor solution may lead to adsorption of the polymer on the carbon electrode surface, causing an increased carbon/electrolyte interfacial resistance. This possibility is expected to depend strongly on the detailed nature of the pore structure and surface chemical functionalization of each carbon paper, and is worthy of further investigation. Alternatively, differing degrees of pore mouth blockage among the various carbon papers by the cross-linked PEGDA scaffold may also lead to unexpected relative changes in ESR when switching from the neat ionic liquid to an ionogel electrolyte. Given that the two-electrode double layer capacitance of both the neat EMI TFSI as well as the ionogel electrolyte is approximately 5 mF cm-2 for planar electrodes [6], it is clear that the ionogel precursor solution did not fully penetrate the porous structure of any of these carbon papers during the test bed fabrication procedure (as demonstrated by the low gravimetric capacitance values measured by CV, Table 2). In addition, the high ESR values observed for these devices may also have limited the gravimetric capacitance values achieved. A modified test bed fabrication protocol wherein the iono gel precursor solution is actively drawn into the porous carbon papers (i.e. by vacuum filling) is currently being developed in order to increase the gravimetric capacitance values and to clarify the issue of seeming unpredictable relative ESR changes when transitioning from an ionic liquid to an ionogel electrolyte.

    4. Conclusion

    In order to begin integrating UV-cured solid ionogel electrolytes, a promising class of emergent materials for supercapacitors, with high surface area carbon paper electrodes in situ, an underst and ing of the relative compatibility of the ionogel with different carbon electrode materials is required. The coplanar test bed geometry utilized here represents one schema by which this integration might be achieved, and it also provides a straightforward way to compare the electrical response of an ionogel electrolyte with its neat ionic liquid analog. Furthermore, initial results using this test bed have revealed anomalous trends in the relative increase of device equivalent series resistance observed for the use of a 16 wt% PEGDA ionogel compared to the neat ionic liquid that highlight the need to better underst and the wetting and interfacial surface behavior at the electrode/electrolyte interface. These findings can help guide future efforts regarding the in situ integration of ionogel electrolytes with porous carbon electrodes for wearable energy storage applications.

    Acknowledgments

    The authors wish to acknowledge Adam Visentin and Ariel Horowitz for useful discussions, Dr. Anna Osherov for collecting the SEM images, and Changqiong Zhu for measuring the carbon paper sheet resistances. SEM images and sheet resistance values were obtained at the Center for Nanoscale Systems (CNS), a member of the National Nanotechnology Infrastructure Network (NNIN), which is supported by the National Science Foundation under NSF award no. ECS-0335765. CNS is part of Harvard University. The authors gratefully acknowledge financial support from the Science, Mathematics and Research for Transformation scholarship, the US Army Natick Soldier Research, Development and Engineering Center, and the National Science Foundation (award no. ECCS-1201935).

    Conflict of interest

    All authors declare no conflicts of interest in this paper.



    [1] Hersh B, Mirkouei A, Sessions J, et al. (2019) A Review and Future Directions on Enhancing Sustainability Benefits across Food-Energy-Water Systems: The Potential Role of Biochar-Derived Products. AIMS Environ Sci 6: 379–416. https://doi.org/10.3934/environsci.2019.5.379 doi: 10.3934/environsci.2019.5.379
    [2] Yang X, Chen S. (2021) Microorganisms in Sediment Microbial Fuel Cells: Ecological Niche, Microbial Response, and Environmental Function. Sci. Total Environ 756: 144145. https://doi.org/10.1016/j.scitotenv.2020.144145 doi: 10.1016/j.scitotenv.2020.144145
    [3] Miramontes-Viña V, Romero-Castro N, López-Cabarcos M Á. (2023) Advancing towards a Sustainable Energy Model. Uncovering the Untapped Potential of Rural Areas. AIMS Environ Sci 10: 287–312. https://doi.org/10.3934/environsci.2023017 doi: 10.3934/environsci.2023017
    [4] Srivastava R K, Boddula R, Pothu R. (2022) Microbial Fuel Cells: Technologically Advanced Devices and Approach for Sustainable/Renewable Energy Development. Energy Convers Manag X: 13: 100160. https://doi.org/10.1016/j.ecmx.2021.100160 doi: 10.1016/j.ecmx.2021.100160
    [5] Darmawan R, Juliastuti S R, Hendrianie N, et al. (2022) Effect of Electrode Modification on the Production of Electrical Energy and Degradation of Cr (Ⅵ) Waste Using Tubular Microbial Fuel Cell. AIMS Environ Sci 9: 505–525. https://doi.org/10.3934/environsci.2022030 doi: 10.3934/environsci.2022030
    [6] Xin S, Shen J, Liu G, et al. (2022) Electricity Generation and Microbial Community of Single-Chamber Microbial Fuel Cells in Response to Cu2O Nanoparticles/Reduced Graphene Oxide as Cathode Catalyst. Chem Eng J 380: 122446. https://doi.org/10.1016/j.cej.2019.122446 doi: 10.1016/j.cej.2019.122446
    [7] Pant D, Van Bogaert G, Diels L, et al. (2010) A Review of the Substrates Used in Microbial Fuel Cells (MFCs) for Sustainable Energy Production. Bioresour. Technol 101: 1533–1543. https://doi.org/10.1016/j.biortech.2009.10.017 doi: 10.1016/j.biortech.2009.10.017
    [8] Guambo A, Calderón C, Paña S, et al. (2021) Bioelectricity Production with Organic Substrates, Nitrates and Lead Using High Andean Soils. Adv Intell Syst Comput 1277: 198–208. https://doi.org/10.1007/978-3-030-60467-7_17 doi: 10.1007/978-3-030-60467-7_17
    [9] Arulmani S R B, Gnanamuthu H L, Kandasamy S, et al. (2021) Sustainable Bioelectricity Production from Amaranthus Viridis and Triticum Aestivum Mediated Plant Microbial Fuel Cells with Efficient Electrogenic Bacteria Selections. Process Biochem 107. https://doi.org/10.1016/j.procbio.2021.04.015 doi: 10.1016/j.procbio.2021.04.015
    [10] Nguyen H D, Babel S. (2023) A Novel Coupled Microbial Fuel Cell Operation for Organic and Nitrogen Removal with Simultaneous Energy Recovery from Wastewater. Sustain Energy Technol Assessments 55: 102981. https://doi.org/10.1016/j.seta.2022.102981 doi: 10.1016/j.seta.2022.102981
    [11] Bajracharya S. (2020) Microbial Fuel Cell Coupled with Anaerobic Treatment Processes for Wastewater Treatment. Integr Microb Fuel Cells Wastewater Treat 295–311. ttps://doi.org/10.1016/B978-0-12-817493-7.00014-X doi: 10.1016/B978-0-12-817493-7.00014-X
    [12] Wrighton K C, Agbo P, Warnecke F, et al. (2008) A Novel Ecological Role of the Firmicutes Identified in Thermophilic Microbial Fuel Cells. ISME J 2: 1146–1156. https://doi.org/10.1038/ismej.2008.48 doi: 10.1038/ismej.2008.48
    [13] Zhang G, Feng S, Jiao Y, et al. (2017) Cathodic Reducing Bacteria of Dual-Chambered Microbial Fuel Cell. Int J Hydrogen Energy 42: 27607–27617. https://doi.org/10.1016/j.ijhydene.2017.06.095 doi: 10.1016/j.ijhydene.2017.06.095
    [14] Zhang G, Zhao Q, Jiao Y, et al. (2012) Biocathode Microbial Fuel Cell for Efficient Electricity Recovery from Dairy Manure. Biosens Bioelectron 31. https://doi.org/10.1016/j.bios.2011.11.036 doi: 10.1016/j.bios.2011.11.036
    [15] Chen C Y, Chen T Y, Chung Y C A (2014) Comparison of Bioelectricity in Microbial Fuel Cells with Aerobic and Anaerobic Anodes. Environ Technol 35. https://doi.org/10.1080/09593330.2013.826254 doi: 10.1080/09593330.2013.826254
    [16] Erensoy A, Mulayim S, Orhan A, et al. (2022) The System Design of the Peat-Based Microbial Fuel Cell as a New Renewable Energy Source: The Potential and Limitations. Alexandria Eng J 61: 8743–8750. https://doi.org/10.1016/j.aej.2022.02.020 doi: 10.1016/j.aej.2022.02.020
    [17] Szydlowski L, Lan T C T, Shibata N, et al. (2020) Metabolic Engineering of a Novel Strain of Electrogenic Bacterium Arcobacter Butzleri to Create a Platform for Single Analyte Detection Using a Microbial Fuel Cell. Enzyme Microb Technol 139: 109564. https://doi.org/10.1016/j.enzmictec.2020.109564 doi: 10.1016/j.enzmictec.2020.109564
    [18] Krithika T, Kavitha R, Dinesh M, et al. (2021) Assessment of Ligninolytic Bacterial Consortium for the Degradation of Azo Dye with Electricity Generation in a Dual-Chambered Microbial Fuel Cell. Environ Challenges 4: 100093. https://doi.org/10.1016/j.envc.2021.100093 doi: 10.1016/j.envc.2021.100093
    [19] Gupta P, Pandey K, Verma N. (2021) Improved Oxygen Reduction and Simultaneous Glyphosate Degradation over Iron Phthalocyanine and Reduced Graphene Oxide‒dispersed Activated Carbon Fiber Electrodes in a Microbial Fuel Cell. J Power Sources 514. https://doi.org/10.1016/j.jpowsour.2021.230592 doi: 10.1016/j.jpowsour.2021.230592
    [20] Ambaye T G, Vaccari M, Franzetti A, et al. (2023) Microbial Electrochemical Bioremediation of Petroleum Hydrocarbons (PHCs) Pollution: Recent Advances and Outlook. Chem Eng J 452. https://doi.org/10.1016/j.cej.2022.139372 doi: 10.1016/j.cej.2022.139372
    [21] Fatehbasharzad P, Aliasghari S, Tabrizi I S, et al. (2022) Microbial Fuel Cell Applications for Removal of Petroleum Hydrocarbon Pollutants: A Review. Water Resour Ind 28: 100178. https://doi.org/10.1016/j.wri.2022.100178 doi: 10.1016/j.wri.2022.100178
    [22] Puig S, Serra M, Coma M, et al. (2011) Microbial Fuel Cell Application in Landfill Leachate Treatment. J Hazard Mater 185. https://doi.org/10.1016/j.jhazmat.2010.09.086 doi: 10.1016/j.jhazmat.2010.09.086
    [23] Biffinger J C, Pietron J, Ray R, et al. (2007) A Biofilm Enhanced Miniature Microbial Fuel Cell Using Shewanella Oneidensis DSP10 and Oxygen Reduction Cathodes. Biosens Bioelectron 22: 1672–1679. https://doi.org/10.1016/j.bios.2006.07.027 doi: 10.1016/j.bios.2006.07.027
    [24] Pu K B, Li T T, Gao J Y, et al. (2022) Floating Flexible Microbial Fuel Cells for Electricity Generation and Municipal Wastewater Treatment. Sep Purif Technol 300. https://doi.org/10.1016/j.seppur.2022.121915 doi: 10.1016/j.seppur.2022.121915
    [25] Ghangrekar M M, Shinde V B. (2007) Performance of Membrane-Less Microbial Fuel Cell Treating Wastewater and Effect of Electrode Distance and Area on Electricity Production. Bioresour Technol 98: 2879–2885. https://doi.org/10.1016/j.biortech.2006.09.050 doi: 10.1016/j.biortech.2006.09.050
    [26] Xu J, Sheng G P, Luo H W, et al. (2012) Fouling of Proton Exchange Membrane (PEM) Deteriorates the Performance of Microbial Fuel Cell. Water Res 46: 1817–1824. https://doi.org/10.1016/j.watres.2011.12.060 doi: 10.1016/j.watres.2011.12.060
    [27] Kondaveeti S, Lee J, Kakarla R, et al. (2014) Low-Cost Separators for Enhanced Power Production and Field Application of Microbial Fuel Cells (MFCs). Electrochim Acta 132: 434–440. https://doi.org/10.1016/j.electacta.2014.03.046 doi: 10.1016/j.electacta.2014.03.046
    [28] Li D, Feng Y, Li F, et al. (2023) Carbon Fibers for Bioelectrochemical: Precursors, Bioelectrochemical System, and Biosensors. Adv Fiber Mater 5: 699–730. https://doi.org/10.1007/s42765-023-00256-w doi: 10.1007/s42765-023-00256-w
    [29] Shirvanimoghaddam K, Hamim S U, Akbari M K, et al. (2017) Carbon Fiber Reinforced Metal Matrix Composites: Fabrication Processes and Properties. Compos. Part A Appl Sci Manuf 92: 70–96. https://doi.org/10.1016/j.compositesa.2016.10.032 doi: 10.1016/j.compositesa.2016.10.032
    [30] Oroumei A, Naebe M. (2017) Mechanical Property Optimization of Wet-Spun Lignin/Polyacrylonitrile Carbon Fiber Precursor by Response Surface Methodology. Fibers Polym 18. https://doi.org/10.1007/s12221-017-7363-9 doi: 10.1007/s12221-017-7363-9
    [31] Djellali M, Kameche M, Kebaili H, et al. (2021) Synthesis of Nickel-Based Layered Double Hydroxide (LDH) and Their Adsorption on Carbon Felt Fibres: Application as Low Cost Cathode Catalyst in Microbial Fuel Cell (MFC). Environ Technol 42. https://doi.org/10.1080/09593330.2019.1635652 doi: 10.1080/09593330.2019.1635652
    [32] Li X, Liu G, Ma F, et al. (2018) Enhanced Power Generation in a Single-Chamber Dynamic Membrane Microbial Fuel Cell Using a Nonstructural Air-Breathing Activated Carbon Fiber Felt Cathode. Energy Convers Manag 172. https://doi.org/10.1016/j.enconman.2018.07.011 doi: 10.1016/j.enconman.2018.07.011
    [33] Jiang D, Chen H, Xie H, et al. (2023) Fe, N, S Co-Doped Cellulose Paper Carbon Fibers as an Air-Cathode Catalyst for Microbial Fuel Cells. Environ Res 221. https://doi.org/10.1016/j.envres.2023.115308 doi: 10.1016/j.envres.2023.115308
    [34] Yan S, Xiong W, Xing S, et al. (2017) Oxidation of Organic Contaminant in a Self-Driven Electro/Natural Maghemite/Peroxydisulfate System: Efficiency and Mechanism. Sci Total Environ 599–600. https://doi.org/10.1016/j.scitotenv.2017.05.037 doi: 10.1016/j.scitotenv.2017.05.037
    [35] Khalifa A Y Z, Almalki M. (2019) Polyphasic Characterization of Delftia Acidovorans ESM-1, a Facultative Methylotrophic Bacterium Isolated from Rhizosphere of Eruca Sativa. Saudi J Biol Sci 26. https://doi.org/10.1016/j.sjbs.2018.05.015 doi: 10.1016/j.sjbs.2018.05.015
    [36] Chen Y L, Lee C C, Lin Y L, et al. (2015) Obtaining Long 16S RDNA Sequences Using Multiple Primers and Its Application on Dioxin-Containing Samples. BMC Bioinformatics 16: S13. https://doi.org/10.1186/1471-2105-16-S18-S13 doi: 10.1186/1471-2105-16-S18-S13
    [37] Geer L Y, Marchler-Bauer A, Geer R C, et al.(2009) The NCBI BioSystems Database. Nucleic Acids Res 38. https://doi.org/10.1093/nar/gkp858 doi: 10.1093/nar/gkp858
    [38] Meeker E W, Wagner E C (1933)Titration of Ammonia in Presence of Boric Acid. Ind Eng Chem Anal Ed 5: 396–398. doi: 10.1021/ac50086a012.https://doi.org/10.1021/ac50086a012 doi: 10.1021/ac50086a012
    [39] Standard Methods For the Examination of Water and Wastewater 5210 BIOCHEMICAL OXYGEN DEMAND (BOD). Stand Methods Exam Water Wastewater doi: 10.2105/SMWW.2882.102.
    [40] Wastewater, S.M.F. the E. of W. and 5220 CHEMICAL OXYGEN DEMAND (COD). Stand. Methods Exam. Water Wastewater.
    [41] Wastewater, S.M.F. the E. of W. and 4500-H+ PH. Stand. Methods Exam. Water Wastewater.
    [42] Zhang C F, Zhong X C, Yu H Y, et al. (2009) Effects of Cobalt Doping on the Microstructure and Magnetic Properties of Mn-Zn Ferrites Prepared by the Co-Precipitation Method. Phys B Condens Matter 404: 2327–2331. https://doi.org/10.1016/j.physb.2008.12.044 doi: 10.1016/j.physb.2008.12.044
    [43] Silva C, Borbáth I, Zelenka K, et al. (2022) Effect of the Reductive Treatment on the State and Electrocatalytic Behavior of Pt in Catalysts Supported on Ti0.8Mo0.2O2-C Composite. React Kinet Mech Catal 135: 29–47. https://doi.org/10.1007/s11144-021-02131-4 doi: 10.1007/s11144-021-02131-4
    [44] Pászti Z, Hakkel O, Keszthelyi T, et al. (2010) Interaction of Carbon Monoxide with Au(111) Modified by Ion Bombardment: A Surface Spectroscopy Study under Elevated Pressure. Langmuir 26: 16312–16324. https://doi.org/10.1021/la1014913 doi: 10.1021/la1014913
    [45] N. Fairley CasaXPS: Spectrum Processing Software for XPS, AES and SIMS. Cheshiree.
    [46] Diczházi D, Borbáth I, Bakos I, et al. (2021) Design of Mo-Doped Mixed Oxide–Carbon Composite Supports for Pt-Based Electrocatalysts: The Nature of the Mo-Pt Interaction. Catal Today 366: 31–40. https://doi.org/10.1016/j.cattod.2020.04.004 doi: 10.1016/j.cattod.2020.04.004
    [47] Mohai, M. XPS MultiQuant: Multi-Model X-Ray Photoelectron Spectroscopy Quantification Program. Version 7.00.92. 2011.
    [48] Mohai, M. XPS MultiQuant: Multimodel XPS Quantification Software. Surf Interface Anal 36: 828–832. https://doi.org/10.1002/sia.1775
    [49] Zhang J, Li J, Ye D, et al. (2014) Enhanced Performances of Microbial Fuel Cells Using Surface-Modified Carbon Cloth Anodes: A Comparative Study. Int J Hydrogen Energy 39: 19148–19155. https://doi.org/10.1016/j.ijhydene.2014.09.067 doi: 10.1016/j.ijhydene.2014.09.067
    [50] Feng Y, Yang Q, Wang X, et al. (2010) Treatment of Carbon Fiber Brush Anodes for Improving Power Generation in Air–Cathode Microbial Fuel Cells. J Power Sources 195: 1841–1844. https://doi.org/10.1016/j.jpowsour.2009.10.030 doi: 10.1016/j.jpowsour.2009.10.030
    [51] Karami M, McMorrow G V, Wang L (2018) Continuous Monitoring of Indoor Environmental Quality Using an Arduino-Based Data Acquisition System. J Build Eng 19. https://doi.org/10.1016/j.jobe.2018.05.014 doi: 10.1016/j.jobe.2018.05.014
    [52] Escapa A, Gil-Carrera L, García V, et al. (2012) Performance of a Continuous Flow Microbial Electrolysis Cell (MEC) Fed with Domestic Wastewater. Bioresour Technol 117.
    [53] Nanda A, Mohapatra B B, Mahapatra A P K, et al. (2021) Multiple Comparison Test by Tukey's Honestly Significant Difference (HSD): Do the Confident Level Control Type I Error. Int J Stat Appl Math 6. https://doi.org/10.22271/maths.2021.v6.i1a.636 doi: 10.22271/maths.2021.v6.i1a.636
    [54] Feng S, Hou S, Huang X, et al. (2019) Insights into the Microbial Community Structure of Anaerobic Digestion of Municipal Solid Waste Landfill Leachate for Methane Production by Adaptive Thermophilic Granular Sludge. Electron J Biotechnol 39. https://doi.org/10.1016/j.ejbt.2019.04.001 doi: 10.1016/j.ejbt.2019.04.001
    [55] Ghosh P, Gupta A, Thakur I S. (2015) Combined Chemical and Toxicological Evaluation of Leachate from Municipal Solid Waste Landfill Sites of Delhi, India. Environ Sci Pollut Res 22. https://doi.org/10.1007/s11356-015-4077-7 doi: 10.1007/s11356-015-4077-7
    [56] MAE TULSMA Available online: https://www.ambiente.gob.ec/wp-content/uploads/downloads/2018/05/TULSMA.pdf (accessed on 2 October 2023).
    [57] Saeed T, Yadav A K, Miah M J (2022) Landfill Leachate and Municipal Wastewater Co-Treatment in Microbial Fuel Cell Integrated Unsaturated and Partially Saturated Tidal Flow Constructed Wetlands. J Water Process Eng 46. https://doi.org/10.1016/j.jwpe.2022.102633 doi: 10.1016/j.jwpe.2022.102633
    [58] Kumar S S, Kumar A, Malyan S K, et al. (2023) Landfill Leachate Valorization: A Potential Alternative to Burden off Resources and Support Energy Systems. Fuel 331. https://doi.org/10.1016/j.fuel.2022.125911 doi: 10.1016/j.fuel.2022.125911
    [59] Hassan M, Wei H, Qiu H, et al. (2018) Power Generation and Pollutants Removal from Landfill Leachate in Microbial Fuel Cell: Variation and Influence of Anodic Microbiomes. Bioresour Technol 247. https://doi.org/10.1016/j.biortech.2017.09.124 doi: 10.1016/j.biortech.2017.09.124
    [60] Li X, Lu Y, Luo H, et al. (2021) Effect of PH on Bacterial Distributions within Cathodic Biofilm of the Microbial Fuel Cell with Maltodextrin as the Substrate. Chemosphere 265. https://doi.org/10.1016/j.chemosphere.2020.129088 doi: 10.1016/j.chemosphere.2020.129088
    [61] Singh M, Ulbrich P, Prokopec V, et al. (2013) Vapour Phase Approach for Iron Oxide Nanoparticle Synthesis from Solid Precursors. J Solid State Chem 200: 150–156. https://doi.org/10.1016/j.jssc.2013.01.037 doi: 10.1016/j.jssc.2013.01.037
    [62] Asuha S, Zhao Y M, Zhao S, et al. (2012) Synthesis of Mesoporous Maghemite with High Surface Area and Its Adsorptive Properties. Solid State Sci 14: 833–839. https://doi.org/10.1016/j.solidstatesciences.2012.04.011 doi: 10.1016/j.solidstatesciences.2012.04.011
    [63] Trushkina Y, Tai C W, Salazar-Alvarez G. (2019) Fabrication of Maghemite Nanoparticles with High Surface Area. Nanomaterials 9. https://doi.org/10.3390/nano9071004 doi: 10.3390/nano9071004
    [64] Guivar J A R, Sadrollahi E, Menzel D, et al. Magnetic, Structural and Surface Properties of Functionalized Maghemite Nanoparticles for Copper and Lead Adsorption. RSC Adv 7: 28763–28779, https://doi.org/10.1039/C7RA02750H doi: 10.1039/C7RA02750H
    [65] Patekari M D, Pawar K K, Salunkhe G B, et al. (2021) Synthesis of Maghemite Nanoparticles for Highly Sensitive and Selective NO2 Sensing. Mater Sci Eng B Solid-State Mater Adv Technol 272: 115339. https://doi.org/10.1016/j.mseb.2021.115339 doi: 10.1016/j.mseb.2021.115339
    [66] Cao D, Li H, Pan L, et al. High Saturation Magnetization of γ 3-Fe2 O3 Nano-Particles by a Facile One-Step Synthesis Approach. Sci Rep 6: 1–9. https://doi.org/10.1038/srep32360 doi: 10.1038/srep32360
    [67] Shetty A R, de Gannes V, Obi C C, et al. (2015) Complete Genome Sequence of the Phenanthrene-Degrading Soil Bacterium Delftia Acidovorans Cs1-4. Stand Genomic Sci 10. https://doi.org/10.1186/s40793-015-0041-x doi: 10.1186/s40793-015-0041-x
    [68] Morel M A, Ubalde M C, Braña V, et al. (2011) Delftia Sp. JD2: A Potential Cr(Ⅵ)-Reducing Agent with Plant Growth-Promoting Activity. Arch Microbiol 193. https://doi.org/10.1007/s00203-010-0632-2 doi: 10.1007/s00203-010-0632-2
    [69] Leibeling S, Schmidt F, Jehmlich N, et al. (2010) Declining Capacity of Starving Delftia Acidovorans MC1 to Degrade Phenoxypropionate Herbicides Correlates with Oxidative Modification of the Initial Enzyme. Environ Sci Technol 44. https://doi.org/10.1021/es903619j doi: 10.1021/es903619j
    [70] Morel M A, Iriarte A, Jara Tellechea E S, et al. (2016) Revealing the Biotechnological Potential of Delftia Sp. JD2 by a Genomic Approach. AIMS Bioeng 3: 156–175. https://doi.org/10.3934/bioeng.2016.2.156 doi: 10.3934/bioeng.2016.2.156
    [71] Nosek D, Samsel O, Pokój T, et al. (2023) Waste Volatile Fatty Acids as a Good Electron Donor in Microbial Fuel Cell with the Iron-Modified Anode. Int J Environ Sci Technol 20. https://doi.org/10.1007/s13762-023-04850-8 doi: 10.1007/s13762-023-04850-8
    [72] Ishii S, Logan B E, Sekiguchi Y. (2012) Enhanced Electrode-Reducing Rate during the Enrichment Process in an Air-Cathode Microbial Fuel Cell. Appl Microbiol Biotechnol 94. https://doi.org/10.1007/s00253-011-3844-8 doi: 10.1007/s00253-011-3844-8
    [73] Jangir Y, French S, Momper L M, et al. (2016) Isolation and Characterization of Electrochemically Active Subsurface Delftia and Azonexus Species. Front Microbiol 7. https://doi.org/10.3389/fmicb.2016.00756 doi: 10.3389/fmicb.2016.00756
    [74] Malyan S K, Kumar S S, Fagodiya R K, et al. (2021) Biochar for Environmental Sustainability in the Energy-Water-Agroecosystem Nexus. Renew. Sustain. Energy Rev 149: 111379. https://doi.org/10.1016/j.rser.2021.111379 doi: 10.1016/j.rser.2021.111379
    [75] Saeed T, Miah M J, Yadav A K (2022) Development of Electrodes Integrated Hybrid Constructed Wetlands Using Organic, Construction, and Rejected Materials as Filter Media: Landfill Leachate Treatment. Chemosphere 303. https://doi.org/10.1016/j.chemosphere.2022.135273 doi: 10.1016/j.chemosphere.2022.135273
    [76] Vu M T, Noori M T, Min B. (2020) Magnetite/Zeolite Nanocomposite-Modified Cathode for Enhancing Methane Generation in Microbial Electrochemical Systems. Chem Eng J 393. https://doi.org/10.1016/j.cej.2020.124613 doi: 10.1016/j.cej.2020.124613
    [77] Omidi M, Mashkour M, Biswas J K, et al. (2021) From Electricity to Products: Recent Updates on Microbial Electrosynthesis (MES). Top Catal https://doi.org/10.1007/s11244-021-01503-3 doi: 10.1007/s11244-021-01503-3
    [78] Liu P, Liang P, Jiang Y, et al. (2018) Stimulated Electron Transfer inside Electroactive Biofilm by Magnetite for Increased Performance Microbial Fuel Cell. Appl Energy 216. https://doi.org/10.1016/j.apenergy.2018.01.073 doi: 10.1016/j.apenergy.2018.01.073
    [79] Nouri P, Najafpour Darzi G. (2017) Impacts of Process Parameters Optimization on the Performance of the Annular Single Chamber Microbial Fuel Cell in Wastewater Treatment. Eng Life Sci 17 https://doi.org/10.1002/elsc.201600173 doi: 10.1002/elsc.201600173
  • This article has been cited by:

    1. Stephanie Flores Zopf, Michael Manser, Screen-printed Military Textiles for Wearable Energy Storage, 2016, 11, 1558-9250, 155892501601100, 10.1177/155892501601100303
    2. M. Aulice Scibioh, B. Viswanathan, 2020, 9780128198582, 35, 10.1016/B978-0-12-819858-2.00003-2
    3. Rajib Paul, Ajit K. Roy, Liming Dai, 2021, 9780128191170, 143, 10.1016/B978-0-12-819117-0.00001-2
    4. Nerea Gil-González, T. Akyazi, E. Castaño, F. Benito-Lopez, Maria C. Morant-Miñana, Elucidating the role of the ionic liquid in the actuation behavior of thermo-responsive ionogels, 2018, 260, 09254005, 380, 10.1016/j.snb.2017.12.153
    5. Xuli Chen, Rajib Paul, Liming Dai, Carbon-based supercapacitors for efficient energy storage, 2017, 4, 2095-5138, 453, 10.1093/nsr/nwx009
    6. Minh-Hai Tran, Hae Kyung Jeong, Ternary carbon composite films for supercapacitor applications, 2017, 684, 00092614, 1, 10.1016/j.cplett.2017.06.025
    7. Shaun Whitley, Dowon Bae, Perspective—Insights into Solar-Rechargeable Redox Flow Cell Design: A Practical Perspective for Lab-Scale Experiments, 2021, 168, 0013-4651, 120517, 10.1149/1945-7111/ac3ab3
    8. Asim Ali Yaqoob, Mohamad Nasir Mohamad Ibrahim, Khalid Umar, Tabassum Parveen, Akil Ahmad, David Lokhat, Siti Hamidah Mohd Setapar, A glimpse into the microbial fuel cells for wastewater treatment with energy generation, 2021, 214, 19443986, 379, 10.5004/dwt.2021.26737
    9. Swetha Vasudevan Kanakkottu, Babak Rezaei, Stephan Sylvest Keller, Metal-free on-chip microsupercapacitor with high-aspect-ratio 3D interdigitated pyrolytic carbon microelectrodes derived from additive manufacturing, 2025, 641, 03787753, 236816, 10.1016/j.jpowsour.2025.236816
  • Reader Comments
  • © 2023 the Author(s), licensee AIMS Press. This is an open access article distributed under the terms of the Creative Commons Attribution License (http://creativecommons.org/licenses/by/4.0)
通讯作者: 陈斌, bchen63@163.com
  • 1. 

    沈阳化工大学材料科学与工程学院 沈阳 110142

  1. 本站搜索
  2. 百度学术搜索
  3. 万方数据库搜索
  4. CNKI搜索

Metrics

Article views(1714) PDF downloads(94) Cited by(1)

Article outline

Figures and Tables

Figures(9)  /  Tables(4)

/

DownLoad:  Full-Size Img  PowerPoint
Return
Return

Catalog