2 Maximising electricity production by controlling the biofilm specific growth rate in Microbial Fuel Cells 4 Pablo Ledezma1*, John Greenman2 and Ioannis Ieropoulos1 1 6 Bristol Robotics Laboratory, Universities of Bristol and of the West of England, Frenchay Campus, Bristol BS34 8QZ, U.K. 2 Department of Applied Sciences, University of the West of England, Bristol BS16 1QY, U.K. 8 * Corresponding author: pablo.ledezma@brl.ac.uk Telephone: +44 (0) 117 32 86350 10 Fax: +44 (0) 117 32 83960 12 Abstract 14 16 18 20 22 24 The aim of this work is to study the relationship between growth rate and electricity production in perfusion-electrode Microbial Fuel Cells (MFCs), across a wide range of flow rates by comeasurement of electrical output and changes in population numbers by viable counts and optical density. The experiments hereby presented demonstrate, for the first time to the authors’ knowledge, that the anodic biofilm specific growth rate can be determined and controlled in common with other loose matrix perfusion systems. Feeding with nutrient-limiting conditions at a critical flow rate (50.8 mL.h-1) resulted in the first experimental determination of maximum specific growth rate μmax (19.8 .day-1) for Shewanella spp. MFC biofilms, which is considerably higher than those predicted or assumed via mathematical modelling. It is also shown that, under carbon-energy limiting conditions there is a strong direct relationship between growth rate and electrical power output, with μmax coinciding with maximum electrical power production. 26 Keywords 28 Microbial fuel cells; Shewanella oneidensis; specific growth rate 30 1. Introduction 32 Microbial Fuel Cells (MFCs) are an exciting technology for the direct, sustainable recovery of 34 electricity from different organic sources and notably organic wastes. Recently, considerable This is a post-print version of the following article: Ledezma, Pablo, Degrenne, Nicolas, Bevilacqua, Pascal, Buret, François, Allard, Bruno, Greenman, John and Ieropoulos, Ioannis (2014) Dynamic polarisation reveals differential steady-state stabilisation and capacitive-like behaviour in microbial fuel cells. Sustainable Energy Technologies and Assessments, 5 1-6. doi:10.1016/j.seta.2013.10.008 research effort has been put into the composition and configuration of these systems, with 36 numerous publications appearing frequently. However, it is not often reported that ultimately it is the microbial cells, growing as a biofilm inside the fuel cell, that generate the electrons depending 38 on their metabolic rates. Understanding growth and metabolism is key to controlling the reactions that occur inside the system and dictate the performance, especially for practical applications. For 40 example, in the case of MFCs for wastewater treatment, knowing the bacterial specific growth rate μ is fundamental, as in any other biological treatment processes, for optimal calibration of the 42 operational settings (Pollard & Greenfield, 1997). It has been said that a good wastewater treatment plant has the inherent ability to exploit the growth of the bacterial population, so that it converts 44 waste to products and biomass in the desired proportions (Henze, 2007). A similar reasoning can be applied to MFCs: the right operational settings can lead to a desired proportion of biomass 46 production and respiration via the anode; maximising the latter is of outmost importance for MFCs employed as a bioelectrochemical power source. 48 Helmstetter and Cummings (1963) first demonstrated that synchronous populations of bacteria, based on dynamic steady-states, could be obtained from a biofilm; their work also showcased the 50 possibility to precisely control the growth rate and physicochemical parameters in a similar way to that achieved in a chemostat, providing that the attachment matrix allowed for homogeneous 52 perfusion of fresh nutrient medium to all cells (Gilbert et al., 1989). MFCs based on carbon veil electrodes have already demonstrated such dynamic steady states (Greenman et al., 2006). The 54 present study describes, for the first time to the authors’ knowledge, measurements of cell production and matrix-electrode biofilm growth rates, revealing a strong relationship between μ and 56 electricity production in MFCs. 58 2. Material and methods This is a post-print version of the following article: Ledezma, Pablo, Degrenne, Nicolas, Bevilacqua, Pascal, Buret, François, Allard, Bruno, Greenman, John and Ieropoulos, Ioannis (2014) Dynamic polarisation reveals differential steady-state stabilisation and capacitive-like behaviour in microbial fuel cells. Sustainable Energy Technologies and Assessments, 5 1-6. doi:10.1016/j.seta.2013.10.008 2.1 MFC assembly and operation 60 Eight standard 20mL/side two-chamber MFCs fabricated via rapid-prototyping (Ledezma et al., 2010) with 270 cm2 plain carbon veil electrodes (Melhuish et al., 2006), were inoculated with S. oneidensis 62 MR-1 and fed with modified M1 minimal medium based on Myers & Nealson (1988) with 18 mM sodium-DL-lactate as the sole carbon source. The medium was fed continuously, initially at a low 64 flow rate of 7.2 mL.h-1 (hereafter referred to as setting 1) until steady state electrode readings were obtained and perfusion concentrations of daughter cells (cfu.mL-1) were constant (approx. 3 weeks) 66 (data not shown). Subsequently, the flow rate was changed to 14.5, 27.3, 50.8, 72.6 and 94.4 mL.h-1 (settings 2 to 6 respectively) and the effects on μ and power production were determined. The MFCs 68 were fitted with an anti grow-back device placed at the inlet port to ensure that no degradation of the substrate occurred prior entry to the anodic chambers. All experiments were conducted at room 70 temperature 23 ± 2 °C. 2.2 Specific growth rate μ 72 2.2.1. Production rate of daughter cells Once steady states were reached, anolyte samples (2 mL) were collected from the MFCs’ outlet flow 74 ports. A 1mL volume was used to determine optical density at 540 nm (OD540nm). The remaining sample volume was used for triplicate viable counts (cfu.mL-1) by serial 10-fold dilution and spiral- 76 plating (Thorn & Greenman, 2009); by multiplying the latter by the set flow rate (mL.h-1), the production rate of daughter cells eluted into the spent perfusate (cfu.h-1) was determined. 78 2.2.2. Biofilm population The experimental steady-state settings and measurement phases were concluded after 80 approximately 10 weeks, following which the MFCs were disassembled and the electrode biofilms were extracted (Lovley & Phillips, 1988) and processed as in 2.2.1. The determined average number This is a post-print version of the following article: Ledezma, Pablo, Degrenne, Nicolas, Bevilacqua, Pascal, Buret, François, Allard, Bruno, Greenman, John and Ieropoulos, Ioannis (2014) Dynamic polarisation reveals differential steady-state stabilisation and capacitive-like behaviour in microbial fuel cells. Sustainable Energy Technologies and Assessments, 5 1-6. doi:10.1016/j.seta.2013.10.008 82 of cells.mL-1 was multiplied by the total volume of the extraction (40 mL PBS) to obtain the total viable cell population per electrode-biofilm. 84 2.2.3. Calculation of specific growth rate μ 86 The specific growth rate μ of the MFC biofilms at each particular flow rate settings was calculated using the following formula (Greenman et al., 2002): 88 μ (.h-1) = production rate of cells in perfusate (cells.h-1)/biofilm population (total number of cells) 2.2.4. Theoretical framework 90 In the presented MFC systems, the folded carbon-veil electrodes form a structure of 38x28x18.5 mm inside each 20 cm3 chamber, leaving very little void volume available for planktonic growth. The 92 former model is thus based on the assumption that once the loose matrix porous electrode is fully colonised, all suitable attachment sites for electron respiration are saturated. In continuous flow, 94 attached cells exist in a non-cumulative steady state, maintaining a near-constant number (Greenman et al., 2006) in a monolayer or thin film form (Helmstetter & Cummings, 1963), while 96 new cells detach into the perfusate flow. Due to the permeability of carbon veil electrodes, cells are uniformly supplied with rate-limiting nutrients, continuously growing at approximately the same 98 rate, and responding equally to shifts in physicochemical conditions (e.g. changes in hydrodynamic flow), with direct consequences for electricity production. This is in opposition to thick biofilms on 100 impermeable surfaces, where it has been demonstrated that substrate diffusion is reduced, creating gradients that lead to differential metabolic activity and thus a wide distribution of μ depending on 102 the cell’s location within the biofilm (Picioreanu et al., 2007); thin biofilms do not exhibit such behaviour and have already been demonstrated for Shewanella oneidensis (Bretschger et al., 2007). 104 It is also assumed that electron transfer from biofilm to electrode is by conductance rather than by This is a post-print version of the following article: Ledezma, Pablo, Degrenne, Nicolas, Bevilacqua, Pascal, Buret, François, Allard, Bruno, Greenman, John and Ieropoulos, Ioannis (2014) Dynamic polarisation reveals differential steady-state stabilisation and capacitive-like behaviour in microbial fuel cells. Sustainable Energy Technologies and Assessments, 5 1-6. doi:10.1016/j.seta.2013.10.008 soluble redox mediators found in the bulk liquid. With the employed flow rates, the Hydraulic 106 Retention Times (HRTs) range from 2.29 to 0.17 h; at moderate and high replacement rates (more than 5 times per hour for setting 6), any mediators would be expected to diffuse and be removed, 108 thus playing no significant role in electricity production over reasonable amounts of time (>10 minutes). 110 2.3 Electrical output 112 MFC voltage output with a 2.2 kΩ external resistor was recorded and the electric power production (in μW) was calculated (Ieropoulos et al., 2008); the load was selected for maximum power 114 production by impedance matching, based on repeated polarisation tests of the MFCs (data not shown). 116 3. Results & Discussion 118 3.1 Effects of flow rate on specific growth rate 120 For non-MFC perfusion biofilm systems in steady state and carbon-energy (C/E) nutrient-limiting conditions, an increase in supply rate has been demonstrated to cause a proportional increase in μ, 122 up to a critical flow rate (CFR), where maximum specific growth rate (μmax) is achieved (Gilbert et al., 1989). Results (Fig. 1) indicate that MFC systems can also exhibit such behaviour. Steady states are 124 demonstrated by constant power output e.g. 42.29 ± 0.06 μW over 8 hours under setting 3, indicative of a stable metabolic activity (see Inset graph, Fig. 1). Separated effluent samplings (see A, 126 B & C in Inset graph, Fig. 1) exhibited near-identical OD540nm (0.563 ± 0.002, 0.561 ± 0.003 and 0.560 This is a post-print version of the following article: Ledezma, Pablo, Degrenne, Nicolas, Bevilacqua, Pascal, Buret, François, Allard, Bruno, Greenman, John and Ieropoulos, Ioannis (2014) Dynamic polarisation reveals differential steady-state stabilisation and capacitive-like behaviour in microbial fuel cells. Sustainable Energy Technologies and Assessments, 5 1-6. doi:10.1016/j.seta.2013.10.008 ± 0.002 respectively; ¼ PBS dilution in all cases). Viable counts then confirmed that the number of 128 cells in the perfusate was stable (A: 1.77 ± 0.14 x 109; C: 1.76 ± 0.15 x 109 cfu.mL-1) while the biofilm extractions performed later on revealed that the populations attached to the electrodes were in the 130 order of ~1011 for all MFCs. The latter evidence confirms the theoretical framework presented in 2.2.4 whereby the grand majority of the cells in the system are attached and respire directly and 132 stably to the electrode, while the electrical output of the planktonic cells (<2% of total cell population in the system, constantly removed by the perfusion flow) by soluble mediators or other 134 means is negligible particularly over large periods of time such as those presented in Fig. 1 Inset. Moreover, a quasi-linear increase in μ up to a CFR (50.82 mL.h-1) was observed in proportion to flow 136 rate (r2= 0.988; p<0.0005). Further increasing the supply rate resulted in no faster growth (see settings 5 and 6, Fig.1); thus, for the particular conditions of these experiments, a μmax of 0.827 ± 138 0.004 .h-1 was reached. To the authors’ knowledge, there are only two previous articles where μmax is reported for bioelectrochemical systems (Lee et al., 2009; Pinto et al., 2010), though both are 140 mathematical estimations and not directly measured or based on real experiments. The biofilm μmax obtained for Shewanella (19.85 .day-1) is 6- or 7-fold higher than calculated in cited papers (3.2 .day-1 142 and 1.97 .day-1 respectively). Results demonstrate accordingly that the specific growth rate of the biofilm inside a MFC can be controlled and maximised (within the limits set by the CFR), as in other 144 perfusion systems, to previously unpredicted levels. 146 3.2 Effects of flow and specific growth rate μ on Power production As depicted in Fig. 2A, an increased flow rate gives a rise in power production up to a limit (a 148 phenomenon also observed by Venkata Mohan et al. (2007) and Behera & Ghangrekar (2009)), which coincides with the CFR for μmax (see setting 4, Fig. 1). Therefore, maximum continuous power This is a post-print version of the following article: Ledezma, Pablo, Degrenne, Nicolas, Bevilacqua, Pascal, Buret, François, Allard, Bruno, Greenman, John and Ieropoulos, Ioannis (2014) Dynamic polarisation reveals differential steady-state stabilisation and capacitive-like behaviour in microbial fuel cells. Sustainable Energy Technologies and Assessments, 5 1-6. doi:10.1016/j.seta.2013.10.008 150 production (Pmax) was recorded when the system was configured to achieve μmax. Steady state outputs were achieved at higher flow rates (and found to be reversible i.e. same power output when 152 the flow-rate was decreased to a previous setting), confirming that the biofilm layers remained attached up to circa 95 mL.h-1 (further research is needed to determine whether shear forces alone 154 are sufficient to remove daughter cells or other shedding mechanisms are involved). Though μ is not synonymous with metabolic rate, the former is ultimately controlled by the latter; at 156 faster growth rates, proton pumping through the lipid membrane would be expected to increase; in the specific case of MFCs, this results in higher electricity production. This positive relationship is 158 depicted in Fig. 2B (fit: r2=0.954; p<0.0005), although confined by the “boundaries” imposed by μmax and Pmax. Flow rates higher than the CFR achieve neither higher power nor growth; this could be 160 explained by: (i) more nutrients passed through the anodic chamber without reaction; (ii) a faster removal of produced H+ (flowing out instead of passing through the PEM); and (iii) Shewanella could 162 not grow any faster under these conditions. It should be noted that said limits are experimentspecific; many other MFC systems exhibit higher electricity production (e.g. with the help of 164 catalysts, non-limiting conditions), but these would still be restricted by μmax. As previously mentioned, determining μ is essential for wastewater treatment systems; the obtained results 166 demonstrate that, under nutrient-limiting conditions, μmax brings about sustainable Pmax. Such mechanisms could therefore be utilised to achieve maximum specific growth rates, for both 168 maximum electricity production and transformation rates of C, N, P, K, Mg (among others) into new biomass. Further research is now needed to determine the behaviour of the system under C/E 170 excess (i.e. limited by a different class of nutrient). 172 Conclusions This is a post-print version of the following article: Ledezma, Pablo, Degrenne, Nicolas, Bevilacqua, Pascal, Buret, François, Allard, Bruno, Greenman, John and Ieropoulos, Ioannis (2014) Dynamic polarisation reveals differential steady-state stabilisation and capacitive-like behaviour in microbial fuel cells. Sustainable Energy Technologies and Assessments, 5 1-6. doi:10.1016/j.seta.2013.10.008 The experiments presented demonstrate that the specific growth rate of bacterial biofilms inside a 174 MFC can be controlled. It is also shown that under C/E-limiting conditions, maximum growth results in maximum power production, with μmax considerably higher than previously estimated. It has been 176 suggested that knowing the growth kinetics of Shewanella oneidensis MR-1 is essential to fully explore its potential in fuel cells (Tang et al., 2007); this is clearly validated here, calling for similar 178 studies for other anodophile species, MFC designs, thick biofilms and conditions other than C/Elimitation so that MFCs can be practically used as bioelectrochemical power sources. 180 Acknowledgements 182 184 186 The authors would like to thank Sam Coupland of the Bristol Robotics Laboratory for his help in the design and fabrication of the MFC parts. Pablo Ledezma is supported by the National Science and Technology Council of Mexico (CONACYT) Ref. 206298. Ioannis Ieropoulos is supported by the Engineering and Physical Sciences Research Council of the UK (EPSRC) CAF EP/I004653/1. 188 190 This is a post-print version of the following article: Ledezma, Pablo, Degrenne, Nicolas, Bevilacqua, Pascal, Buret, François, Allard, Bruno, Greenman, John and Ieropoulos, Ioannis (2014) Dynamic polarisation reveals differential steady-state stabilisation and capacitive-like behaviour in microbial fuel cells. Sustainable Energy Technologies and Assessments, 5 1-6. doi:10.1016/j.seta.2013.10.008 Figures 192 194 Fig. 1. Relationship between flow rate and specific growth rate μ. For data below the CFR, the linear fit is presented. Inset graph: Example of steady power production under flow setting 3. This is a post-print version of the following article: Ledezma, Pablo, Degrenne, Nicolas, Bevilacqua, Pascal, Buret, François, Allard, Bruno, Greenman, John and Ieropoulos, Ioannis (2014) Dynamic polarisation reveals differential steady-state stabilisation and capacitive-like behaviour in microbial fuel cells. Sustainable Energy Technologies and Assessments, 5 1-6. doi:10.1016/j.seta.2013.10.008 196 198 Fig. 2. A: Average power production of MFCs vs perfusate flow rate. B: Average Power production as a function of specific growth rate. Experimental flow rate settings are indicated with numbers (1 to 200 6). This is a post-print version of the following article: Ledezma, Pablo, Degrenne, Nicolas, Bevilacqua, Pascal, Buret, François, Allard, Bruno, Greenman, John and Ieropoulos, Ioannis (2014) Dynamic polarisation reveals differential steady-state stabilisation and capacitive-like behaviour in microbial fuel cells. 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