pH Dependency in Anode Biofilms of Thermincola ferriacetica

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pH Dependency in Anode Biofilms of Thermincola ferriacetica Suggests a Proton-Dependent Electrochemical Response Bradley G. Lusk, Isaias Peraza, Gaurav Albal, Andrew K. Marcus, Sudeep C Popat, and César I. Torres J. Am. Chem. Soc., Just Accepted Manuscript • Publication Date (Web): 12 Apr 2018 Downloaded from http://pubs.acs.org on April 12, 2018

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pH Dependency in Anode Biofilms of Thermincola ferriacetica Suggests a ProtonDependent Electrochemical Response

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Bradley G. Lusk†,¤, Isaias Peraza†, Gaurav Albal†, Andrew K. Marcus†, Sudeep C. Popat*, Cesar I. Torres†,§

6 7 8 9 10 11 12 13 14 15



Swette Center for Environmental Biotechnology, The Biodesign Institute at Arizona State University, P.O. Box 875701, Tempe, Arizona 85287−5701, United States of America ¤

ScienceTheEarth, Mesa, AZ, 85201

*Department of Environmental Engineering and Earth Sciences, Clemson University, 342 Computer Ct, Anderson, SC 29625, United States of America §

School for Engineering of Matter, Transport and Energy, Arizona State University, 501 E Tyler Mall, Tempe, Arizona 85287, United States of America

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Journal of the American Chemical Society

ABSTRACT

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Monitoring the electrochemical response of anode respiring bacteria (ARB) helps

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elucidate the fundamental processes of anode respiration and their rate limitations.

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Understanding these limitations provides insights on how ARB create the complex interfacing of

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biochemical metabolic processes with insoluble electron acceptors and electronics. In this study,

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anode biofilms of the thermophilic (60 oC) Gram-positive ARB Thermincola ferriacetica were

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studied to determine the presence of a proton-dependent electron transfer response. The effects

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of pH, the presence of an electron donor (acetate), and biofilm growth were varied to determine

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their influence on the electrochemical midpoint potential (EKA) and formal redox potential (Eo`)

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under non-turnover conditions. The EKA and Eo` are associated to an enzymatic process within

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ARB’s metabolism that controls the rate and energetic state of their respiration. Results for all

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conditions indicate that pH was the major contributor to altering the energetics of T. ferriacetica

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anode biofilms. Electrochemical responses measured in the absence of an electron donor and

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with a minimal proton gradient within the anode biofilms resulted in a 48 ± 7 mV/ pH unit shift

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in the Eo`, suggesting a proton-dependent rate-limiting process.

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available for anode respiration (< 200 mV when using acetate as electron donor), our results

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provide a new perspective in understanding proton-transport limitations in ARB biofilms, one in

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which ARB are thermodynamically limited by pH gradients. Since the anode biofilms of all

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ARB which perform direct extracellular electron transfer (EET) investigated thus far exhibit an n

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= 1 Nernstian behavior, and because this behavior is affected by changes in pH, we hypothesize

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that the Nernstian response is associated to membrane proteins responsible for proton

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translocation. Finally, this study shows that the EKA and Eo` are a function of pH within the

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physiological range of ARB and thus, given the significant effect pH has on this parameter, we

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recommend reporting the EKA and Eo` of ARB biofilms at a specific bulk pH. 2 ACS Paragon Plus Environment

Given the limited energy

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Key words: Microbial Electrochemical Cell, Nernst-Monod Kinetics, Midpoint Potential, pH,

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Biofilm

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INTRODUCTION For over a century, researchers have attempted to interface biology and electrochemistry

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by connecting cells, enzymes, or cell components to electrodes [1, 2]. These efforts have led to

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research developments on enzymatic and microbial-based technologies centered on bio-

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electricity including microbial electrochemical cells (MxCs) for wastewater treatment [3]

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biosensors for detecting environmental contaminants [4], and self-powered human-implanted

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devices [5]. While most existing technologies rely on synthetic molecules to interface biology

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and electrodes, a unique opportunity arises through the discovery of anode respiring bacteria

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(ARB): a natural, self-assembled, bioelectrochemical interface.

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Understanding how ARB form an electrochemical network will elucidate how to

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efficiently interface biology and electronics, and thus provide insights for technologies based on

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bio-electricity. The study of MxCs, for example, has been an active research area for more than a

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decade [3, 6, 7]; nevertheless, implementation of commercial MxCs is still limited. The

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development of this emerging technology is impacted by the fundamental knowledge of how the

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ARB connect to the MxC anode. Yet, many details of this process are unknown, from the

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complex set of proteins that allows ARB to transport electrons to their outer membrane, to the

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extracellular electron transfer (EET) that leads electrons to the anode surface [8, 9, 10].

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Despite the complexity of microbial metabolism involving anode respiration, many ARB

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including Geobacter sulfurreducens [11], Thermincola ferriacetica [12, 13],

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Thermoanaerobacter pseudethanolicus [14], Geoalkalibacter ferrihydriticus [15], and

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Geoalkalibacter subterraneus [15] exhibit a simple Nernstian response to changes in anode

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potential, which can be modeled with an n = 1 irreversible Nernst-Monod equation [16]. This

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thermodynamic/kinetic response of ARB suggests that a rate-limiting enzymatic reaction 4 ACS Paragon Plus Environment

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controls the overall rate of respiration, and thus current generation in Gram-negative and Gram-

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positive ARB [17, 18]. Through the study of the electrochemical response of ARB, it has been

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assumed that the n =1 reaction was that of a simple electron transfer [16, 19, 20, 21], like that

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carried out by most cytochromes as shown in Equation 1: Mredn−1 → Moxn + e−

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(1)

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Given the importance of cytochromes in the electron transport chain, their involvement in

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transport of electrons to the outer membrane in Gram-negative bacteria, and most likely in EET,

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the assumption that the electrochemical response of ARB follows Equation 1 has been widely

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accepted [16, 19, 20, 21].

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Changes in pH also affect the energetics of ARB metabolism. Due to the nature of their

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respiration, ARB have a net metabolic reaction in which one proton is released per electron, as

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shown by Equation 2:

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CH3COO- + 3H2O  CO2 + HCO3- + 8H+ + 8e-

(2)

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Since the overall oxidation of the electron donor (e.g., acetate) leads to the production of one

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proton per electron, the Nernst equilibrium potential of the electron donor shifts 59.1 mV/ pH

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unit at 30 oC (66.1 mV/ pH unit at 60 oC) [22]. In G. sulfurreducens, the midpoint potentials

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(EKA) (−0.16 V and -0.10 vs SHE) [23] compared to the standard potential of acetate (−0.29 V vs

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SHE) provides less than 200 mV for growth. Thus, a single pH unit increase or decrease

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significantly changes the potential available for ARB growth. However, if the electrochemical

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response of ARB is that of a single electron transfer as in Equation 1, the reaction is proton-

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independent and cyclic voltammograms (CVs) should not change as a function of pH.

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However, [24] reported a shift in the electrochemical response of G. sulfurreducens non-

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turnover (electron-donor depleted) CVs as a function of pH that followed a ~49 mV/ pH unit

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shift. This is the only report that has quantified the shift in EKA in G. sulfurreducens biofilms as

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a function of pH and it is unknown if the catalytic curve also follows the same dependency.

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Nonetheless, the shift in electrochemical response as a function of pH in G. sulfurreducens

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suggests that the electrochemical response is linked to a proton-dependent electron transfer

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reaction [24].

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simultaneous release of a proton and an electron such as the case of quinones as shown in

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Equation 3:

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This proton linkage can be related to the net reaction being linked to the

MnHred → Mox + nH+ + ne−

(3)

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Alternatively, some proteins, mostly those involved in proton translocation at the

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electron-transport chain, will have a pH dependency, known as the redox-Bohr effect, in which

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the protonation of a site within the protein causes a shift in its thermodynamic equilibrium [21,

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25, 26]. Cytochromes within the periplasmic space of G. sulfurreducens, including PpCA and

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PccH, have been shown to have a redox-Bohr effect and have been linked to proton translocation

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for ATP synthesis [27, 28, 29, 30].

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The pH dependency of ARB’s electrochemical response greatly affects the interpretation

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of electron transfer kinetics and the modeling efforts performed so far [16, 19, 20, 31, 32]. It also

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limits the possible biochemical reactions that could be responsible for this electrochemical

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signal, providing new insights on how ARB perform this unique bioelectrochemical interface.

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The redox-pH dependency of individual proteins has been widely studied [25, 27, 28, 29, 30] but

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studying this phenomenon on a complex ARB biofilm network is a major challenge [24].

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We are interested in determining whether the Nernstian response of ARB is proton-

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dependent. For this, we conducted the first systematic study to observe the effects of pH on the

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energetics of anode respiration by ARB under catalytic and non-catalytic conditions. pH

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gradients in ARB biofilms have been widely documented [13, 31, 33] and are known to limit

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current production. Since G. sulfurreducens has a narrow pH range for growth (5.8-8.0) [31,

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34], it would be difficult to document significant pH changes without affecting the physiological

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and metabolic conditions of this ARB. Thus, in this study, we use T. ferriacetica, a thermophilic

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(60 oC) Gram-positive ARB that has shown a decreased response to pH gradients in the anode

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biofilm [13].

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In addition, T. ferriacetica grows in a wider pH range (5.2-8.3) than most known ARB

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[13] and contains 35 multi-heme c-type cytochromes [35]. To assess the pH-dependent response

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of anode biofilms of T. ferriacetica, we used low-scan cyclic voltammetry (LSCV) to determine

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the EKA under catalytic and formal redox potential (Eo) under non-turnover conditions as a

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function of pH. In addition, LSCV was used to monitor the EKA for the anode biofilm as a

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function of biofilm growth - showing that pH-dependency is the major factor influencing shifts

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in the EKA and Eo of T. ferriacetica anode biofilms. We conclude the manuscript with an in depth

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discussion of our understanding of this phenomenon and its implications in the field of

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bioelectrochemistry.

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MATERIALS AND METHODS

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Growth Medium and Culture Conditions. A modified DSMZ Medium 962:

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Thermovenabulum medium was used to grow T. ferriacetica strain 14005 (DSMZ, Braunshweig,

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Germany). The modified medium contained per liter: 3.4 g NaCH3COO•3H2O, 0.33 g NH4Cl , 7 ACS Paragon Plus Environment

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0.33 g K2HPO4, 0.33 g MgCl2•H2O, 0.1 g CaCl2•2H2O, 0.33 g KCl, 0.05 g yeast extract, 1 mL

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selenite−tungstate stock solution (prepared by dissolving 3 mg Na2SeO3•5H2O, 4 mg

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Na2WO4•2H2O, and 0.5g NaOH in 1 L distilled water), Wolfe’s vitamin solution (10 ml), and

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trace elements solution (10 ml). The trace elements solution was composed of the following

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ingredients (DSMZ 141 Methanogenium Medium) in 1 L deionized water: 1.5 g nitrilotriacetic

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acid, 3.0 g MgSO4•7H2O, 0.5 g MnSO4•H2O, 1.0 g NaCl, 0.1g FeSO4•7H2O, 0.18 g

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CoSO4•7H2O, 0.1 g CaCl2•2H2O, 0.18 g ZnSO4•7H2O, 0.01 g CuSO4•5H2O, 0.02 g

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KAl(SO4)2•12H2O, 0.01 g H3BO3, 0.01 g Na2MoO4•2H2O, 0.03 g NiCl2•6H2O, and 0.3 mg

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Na2SeO3•H2O. Medium was prepared in a condenser apparatus under N2:CO2 (80:20) gas

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conditions. Medium was brought to boil and allowed to boil for 15 minutes per liter. Medium

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was stored in 100 ml serum bottles and autoclaved for 15 minutes at 121 °C. ATCC Vitamin

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Solution and NaHCO3 were added after autoclaving; NaHCO3 concentrations were 50 mM for

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each experimental condition. Initial T. ferriacetica stock cultures were grown in 100 ml serum

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bottles containing 10 mM Fe(OH)3 in an Excella E24 Incubator Shaker (New Brunswick

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Scientific) at 60 ºC and 150 RPM. Subsequent cultures were inoculated using culture grown in

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the laboratory.

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H-Type Microbial Electrolysis Cell Construction for All Experiments with T.

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ferriacetica. H-type microbial electrolysis cells (MECs) were constructed and operated in batch.

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Each MEC consisted of two 350 mL compartments separated by an anion exchange membrane

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(AMI 7001, Membranes International, Glen Rock, NJ). For all MECs, operating temperature

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was 60 °C. All MECs contained two cylindrical graphite anodes with varying surface areas and

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an Ag/AgCl reference electrode (BASi MF-2052). Reference potential conversion to a standard

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hydrogen electrode (SHE) was conducted by constructing a two-chambered cell with one

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chamber containing modified DSMZ Medium 962 and the other containing 1M KCl [12, 36].

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Anode potential was poised at -0.06 V vs SHE and current was continuously monitored every

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two minutes using a potentiostat (Princeton Applied Research, Model VMP3, Oak Ridge, TN).

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For all MECs, the anode chambers were mixed via agitation from a magnetic stir bar. The

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cathode consisted of a single cylindrical graphite rod (0.3 cm diameter and a total area of 6.67

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cm2). Cathode pH was adjusted to 12 via addition of NaOH. Gas collection bags were placed on

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the anode compartments to collect volatile products and on the cathode to collect hydrogen.

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Sterile conditions were maintained as reported in [13].

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Effect of pH on Electrochemical Response at Non-turnover Conditions.

T.

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ferriacetica stock cultures (10 ml) from 100 ml serum bottles were used to inoculate MECs.

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Mature biofilms were established on anodes with media containing 50 mM bicarbonate buffer

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and 25 mM acetate. Then, biomass from the biofilms was transferred to subsequent MECs to

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eliminate background response from Fe(OH)3. Anode surface areas were 3.02 and 3.64 cm2.

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After a mature biofilm was established in each reactor, the medium was replaced by flowing 1 L

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(~3 reactor volumes) of 50 mM bicarbonate buffer with no acetate to achieve a current density (j)

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= ~0.05 A m-2. pH was altered by either the addition of HCl or NaOH and at each pH condition,

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after achieving a steady j, LSCV was performed at 1.0 mV s-1 (~45 minutes). Graphs were

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created by performing a baseline subtraction for all conditions and then normalizing to j/jmax. All

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measurements were performed in triplicate. For all conditions, a one-way ANOVA with post-hoc

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Tukey Honest Significant Difference (HSD) test was performed as reported in [13]. Cell viability

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was confirmed in Supporting Information Fig S8 by showing steady current (~0.05 A m-2) for

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~30 minutes after each scan. Positive (unresponsive biofilms) and negative (bare electrode)

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controls are shown in Supporting Information Fig S9. 9 ACS Paragon Plus Environment

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For all non-turnover experiments, Eo was determined by using the mean of the cathodic (Epc) and anodic peaks (Epa) as shown in Equation 4: ° =

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(4)

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Where Eo is the formal redox potential, Epc is the cathodic peak potential, and Epa is the anodic

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peak potential.

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Effect of pH on Electrochemical Response at Catalytic Conditions. MECs were

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inoculated and mature biofilms were established in an identical matter to the non-turnover

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experiments. To determine the effect of pH on EKA of T. ferriacetica, MECs were operated using

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50 mM bicarbonate buffer and 25 mM acetate as the electron donor. Each MEC had an anode

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surface area of 3.89 cm2. At each pH condition, after achieving a steady j, pH was altered by

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either the addition of HCl or NaOH and LSCV was performed at 1.0 mV s-1 (~45 minutes).

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Graphs were plotted as normalized current density, j/jmax. All measurements were performed in

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triplicate. For all conditions, a one-way ANOVA with post-hoc Tukey Honest Significant

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Difference (HSD) test was performed as reported in [13]. Cell viability was confirmed in

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Supporting Information Fig S7 by showing steady current for ~30 minutes after each scan.

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Positive (unresponsive biofilms) and negative (bare electrode) controls are shown in Supporting

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Information Fig S10.

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Effect of Biofilm Growth Stage on T. ferriacetica’s Electrochemical Response. To

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test whether growth was a determining factor in the midpoint potential response, MECs were

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operated using 25 mM acetate, 50 mM bicarbonate. All MECs were inoculated following the

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protocols from the non-turnover and catalytic experiments. MEC anodes had surface area of

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3.89 cm2 and were monitored over 36 hours as j increased from 0 A m-2 to 12.8 A m-2. LSCV 10 ACS Paragon Plus Environment

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was conducted at a scan rate of 1.0 mV s-1 (~45 minutes) at each gain in j of ~1 A m-2. Samples

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were taken for pH at the beginning (j = 1 A m-2) and at the end (j = 12.8 A m-2) of the

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experiment. The impact of the change in current density in young biofilms on EKA was assessed

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by subtracting the impact caused by change in pH (48 ± 7 mV/ pH unit) determined from

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observing the non-catalytic response to change in pH. All measurements were performed in

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triplicate. For all conditions, a one-way ANOVA with post-hoc Tukey Honest Significant

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Difference (HSD) test was performed as reported in [13].

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Determining pH Gradients Inside Thermophilic T. ferriacetica Biofilms. To estimate

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the pH gradients inside the ARB biofilm, we used a modified version of the Nernst–Monod

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equation developed by [16], shown in Equation (5). This kinetic expression uses an empirical

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pH-inhibition function based on the changes of the pH inside the ARB-biofilm [37].

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=   (

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Where qmaxXf is the maximum substrate consumption rate by the T. ferriacetica (mol Ace cm-3

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day-1), S is substrate donor (acetate) concentration (mol m-3), KS,app is the half-saturation constant

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for T. ferriacetica (mol m-3), E4node is the anode potential (V), E◦KA is the potential at which

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current (j) is ½ jmax at pH 6.9 (V), F is the Faraday constant (96485 C mol-1), R is the ideal gas

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constant (8.314 J mol-1 K-1), T is temperature of the system (K), pHbulk is pH in the bulk solution,

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pH is the pH inside the T. ferriacetica biofilm, and pHopt is the optimum pH at which T.

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ferriacetica grows [13, 31]. To simulate the forward scan cyclic voltammetry, the Eanode was

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made a time-dependent variable with the initial value of -0.6 V vs SHE and scan rate of 1.0 mV

222

s-1.



,  

)(



 (

 ( ° $.$&&('('()*+, ) -./0 ) ! "#

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)(

1 2



) (5)

 ( ('('(.3 )

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Journal of the American Chemical Society

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To compute the gradients of acetate, buffer, and pH inside the biofilm, we used Equation

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5 coupled to a set of two time-dependent partial differential equations with diffusion and reaction

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terms for acetate (Equation 6) and bicarbonate buffer in its protonated form (Equation 7):

226

9[;

9>

9

= 9? @ABC 9

9[;