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Original Research ARTICLE

Front. Mar. Sci., 18 February 2020 | https://doi.org/10.3389/fmars.2020.00072

Heterotrophic Bacteria Exhibit a Wide Range of Rates of Extracellular Production and Decay of Hydrogen Peroxide

  • 1The Evergreen State College, Olympia, WA, United States
  • 2Department of Marine Chemistry and Geochemistry, Woods Hole Oceanographic Institution, Woods Hole, MA, United States
  • 3Department of Chemistry and Geochemistry, Colorado School of Mines, Golden, CO, United States

Bacteria have been implicated as both a source and sink of hydrogen peroxide (H2O2), a reactive oxygen species which can both impact microbial growth and participate in the geochemical cycling of trace metals and carbon in natural waters. In this study, simultaneous H2O2 production and decay by twelve species of heterotrophic bacteria were evaluated in both batch and flow-through incubations. While wide species-to-species variability of cell-normalized H2O2 decay rate coefficients [2 × 10–8 to 5 × 10–6 hr–1 (cell mL–1)–1] was observed, these rate coefficients were relatively consistent for a given bacterial species. By contrast, observed production rates (below detection limit to 3 × 102 amol cell–1 hr–1) were more variable even for the same species. Variations based on incubation conditions in some bacterial strains suggest that external conditions may impact extracellular H2O2 levels either through increased extracellular production or leakage of intracellular H2O2. Comparison of H2O2 production rates to previously determined superoxide (O2) production rates suggests that O2 and H2O2 production are not necessarily linked. Rates measured in this study indicate that bacteria could account for a majority of H2O2 decay observed in aqueous systems but likely only make a modest contribution to dark H2O2 production.

Introduction

Hydrogen peroxide (H2O2) is ubiquitous in natural water systems and contributes to the biogeochemical cycling of trace metals. H2O2 production in natural waters was previously thought to occur primarily through the dismutation of photochemically produced superoxide (O2) (Cooper et al., 1988; Shaked et al., 2010) but in recent years it has been shown to occur under dark conditions (Vermilyea et al., 2010a and 2010b; Dixon et al., 2013; Marsico et al., 2015; Zhang et al., 2016a), indicating that other production pathways exists. Experiments comparing H2O2 production of filtered to that of unfiltered natural water samples (e.g., Moffett and Zafiriou, 1990; Vermilyea et al., 2010b; Marsico et al., 2015; Zhang et al., 2016b) suggest that biological production may be a strong contributor to overall H2O2 concentrations in natural waters.

The specific contribution of bacteria to H2O2 production and how it varies at the species level remains untested. Culture studies on (extracellular) biological H2O2 production by marine biota have, to date, focused on phytoplankton such as raphidophytes (see Marshall et al., 2002), coccolithophores (Palenik et al., 1987), and diatoms (Milne et al., 2009; Waring et al., 2010; Schneider et al., 2016; Cho et al., 2017). However, several recent studies (Learman et al., 2011; Diaz et al., 2013; Zhang et al., 2016a; Hansel et al., 2018; Sutherland et al., 2019) have shown that heterotrophic bacteria may be a substantial source of extracellular O2. While O2 is a possible precursor of H2O2, whether these organisms also produce extracellular H2O2 has not been directly explored. Since H2O2 production rates are not necessarily linked to those of O2 (Schneider et al., 2016; Zhang et al., 2016a), known O2 production rates do not allow for estimation of H2O2 production.

The competing processes of H2O2 production and decay occur simultaneously in natural water systems, and H2O2 decay has been strongly linked to biological processes. For instance, 0.2-mm filtration of seawater led to a substantial decrease in decay (Petasne and Zika, 1997; Yuan and Shiller, 2001). Within a freshwater system, small algae (1–12 mm) and bacteria (0.2–1 mm) were found to be responsible for the majority of H2O2 decay (Cooper et al., 1994). Culture studies showed that increasing concentrations of heterotrophic bacteria Vibrio pelagius (Petasne and Zika, 1997), Vibrio alginolyticus, and Enterobacter cloacae (Cooper et al., 1994) increased decay rates, and that the presence of cyanobacterium Synechococcus – rather than secreted enzymes from that organism – was responsible for increased decay in seawater (Petasne and Zika, 1997). Morris et al. (2016) showed that, in seawater samples, many gene transcripts related to hydroperoxidase enzymes were linked to Alphaproteobacteria and Alteromonadales. Morris et al. (2011) has also shown that the abundant marine cyanobacterium Prochlorococcus lacks the ability to degrade H2O2 and instead relies on heterotrophic bacteria to lower H2O2 concentrations to non-toxic levels. Thus, bacterial degradation of H2O2 is likely to be an important control on H2O2 concentrations in many natural waters. However, the variability in the capacity and rates of H2O2 decay among heterotrophic bacteria is currently unknown.

Accordingly, the goal of this study was to compare rates of bacterial H2O2 production and decay across a wide range of species. Twelve species of common heterotrophic bacteria were chosen from among the organisms used by Diaz et al. (2013) to represent a wide phylogenetic diversity and variety of habitats (benthic vs. planktonic; estuarine vs. marine as well as one freshwater bacterium), as well as a wide range of measured extracellular superoxide production rates. Two different methods – a flow-through method similar to that used by Diaz et al. (2013) and a batch-style incubation better suited for evaluating systems with high decay rates – were used to determine H2O2 production rates and decay rate coefficients.

Materials and Methods

Organisms: Growth and Experimental Conditions

All bacterial strains were obtained from the Hansel lab at Woods Hole Oceanographic Institution and are the same cultures used in Diaz et al., 2013 (Table 1). Cultures were inoculated from freezer stocks into the growth medium and incubated at 30°C until mid-exponential phase. An aliquot was then used to start experimental cultures, which were grown to mid-exponential phase, with growth tracked by measuring optical density at 600 nm, before being harvested for the experiment.

TABLE 1
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Table 1. Bacterial strains selected for present study.

Growth and Experimental Conditions

Growth media were either LB medium (Sigma) made with 1 mM HEPES buffer (for S. oneidensis sp. MR-1) or, for all other cultures, a modified K medium (Andersened., 2005) made in 75% artificial seawater (van Waasbergen et al., 1993) as specified in Diaz et al. (2013). Once the cell reached exponential phase, cells were transferred into and analyzed within a minimal assay media to prevent H2O2 production from medium components. The assay media for H2O2 experiments were either deionized water (for S. oneidensis sp. MR-1) or, for the remaining cultures, 75% artificial seawater (NaCl, MgSO4, CaCl2, and KCl as specified in van Waasbergen et al., 1993) containing no additional nutrients.

Cell density of the cultures was determined by counting cells stained with DAPI (4′,6-diamidino-2-phenylindole) under an epifluorescent microscope, using an average count for ten fields of view. An estimated number for metabolically active cells was obtained by assuming the percentages of metabolically active cells were similar to those measured in Diaz et al. (2013) for the same species (49–97% for the twelve species examined in the present study).

H2O2 Detection

H2O2 was measured using the base-catalyzed chemiluminescent reaction with acridinium ester (AE) using a Waterville Analytical FeLume system as described by Cooper et al. (2000) and King et al. (2007). In summary, a slug of sample was pushed into the system by a carrier stream consisting of a catalase-treated (10 U mL–1) solution of sterile assay medium (Table 1) and combined with acridinium ester reagent (5 mM, pH 3) in a mixing tee. Next, the sample/AE mixture combined with carbonate buffer (0.02 M, pH 10.6) in a flow cell. The photons produced by this reaction were then measured by a photomultiplier tube.

A calibration curve consisting of standard additions of H2O2 stock to aliquots of assay medium was implemented at the beginning of each experimental day.

Assessment of H2O2 Production Rates and Recovery Percentages With Flow-Through Methodology

H2O2 production and decay were quantified by measuring the effluent from cells immobilized on a filter, as in Milne et al. (2009) and modified to correct for breakdown of H2O2 by cells as described in Schneider et al. (2016).

For each experimental run, the sterile assay medium indicated in Table 1 flowed through a peristaltic pump at 0.6 mL min–1 over an empty acid-washed 25 mm 0.45-mm cellulose acetate syringe filter (VWR) and directly into the FeLume system until a constant concentration of H2O2 ([H2O2]unspiked, direct) was detected, about 15 min. After 2.50 mL of culture was loaded onto the filter through the intake tube of the peristaltic pump, assay medium was flowed over the cells until a relatively stable signal was produced (about 10–15 min) and [H2O2] of the effluent ([H2O2]unspiked, cells) was measured. Next, assay medium spiked with additional H2O2 was flowed over the cells until steady-state [H2O2] ([H2O2]spiked,cells) could be measured. Finally, the filter was disconnected from the stream so that [H2O2] of the spiked medium ([H2O2]spiked, direct) could be quantified.

Recovery (RecH2O2) for each experimental run was calculated with the equation:

Rec H 2 O 2 = [ H 2 O 2 ] spiked , cells - [ H 2 O 2 ] unspiked , cells [ H 2 O 2 ] spiked , direct - [ H 2 O 2 ] unspiked , direct (1)

The denominator in eq. 1 represents the increase in [H2O2] in the medium due to the addition of the H2O2 spike, and the numerator represents the measured increase in the presence of cells. Calculation of recovery in this manner assumes that the cells on the filter break down the same fraction of H2O2 from both the spiked and the unspiked medium, i.e., that decay is first-order with respect to [H2O2].

The increase in [H2O2] due to the cells’ production, [H2O2]cell (mol L–1) and a cell-normalized production rate PH2O2 (mol cell–1 hr–1) were then calculated with the equations:

[ H 2 O 2 ] cell = [ H 2 O 2 ] unspiked , cells Rec H 2 O 2 - [ H 2 O 2 ] unspiked , direct (2)

and

P H 2 O 2 = [ H 2 O 2 ] c e l l × Q N (3)

where Q is the flow rate (L hr–1), and N is the number on the cells on the filter, calculated from the measured cell density in the experimental culture and the volume of culture loaded onto the filter.

Measurement of H2O2 Production and Decay Rates by Spiked Batch Incubations

The H2O2 production rate (PH2O2) and the pseudo-first order decay coefficient (kloss,H2O2) were determined by comparing the development of [H2O2] over time in batch incubations with different initial [H2O2]. This method is described by Vermilyea et al. (2010b), and will be referred to here as spiked batch incubations. The method was modified as follows to be used with cultures instead of field samples.

5.00 mL aliquots of bacterial culture were centrifuged at 1000 rpm for 10 min, the supernatant was removed, and the cells were resuspended in fresh assay medium indicated in Table 1. Previous experiments with these species and others closely related indicated that the supernatant is primarily cell-free and has similar reactivity (for instance, in terms of superoxide production and Mn(II) oxidation) to that obtained via filtration (0.2 mm) (e.g., Learman et al., 2011; Diaz et al., 2013). Resuspended cultures were combined with additional assay medium and, in some cases, spiked with 5.00 mM H2O2 stock, so that each incubation was performed on a total volume of 40.0 mL. Samples were incubated in sterile syringes (Kendell Mono-Ject 50 mL) with a magnetic stir bar to facilitate mixing. In previous experiments, syringes with rubber-lined plungers were found to contribute to [H2O2] decay after prolonged contact with seawater. The syringes used in these experiments had plastic plungers. Total H2O2 levels for each syringe were analyzed over a period of time necessary for [H2O2] to reach steady state (∼15 min to 2 h, depending on bacterial strain).

To model simultaneous production and decay, it was assumed that the production rate of H2O2 in the medium (mol L–1 h–1), PH2O2, was constant and that both P′H2O2 and the first-order decay rate coefficient k′loss,H2O2 (h–1) are the same in the spiked and unspiked samples:

d [ H 2 O 2 ] dt = P H 2 O 2 - k loss , H 2 O 2 [ H 2 O 2 ] (4)

The solution for this differential equation is:

[ H 2 O 2 ] = P H 2 O 2 k loss , H 2 O 2
- { ( P H 2 O 2 k loss , H 2 O 2 - [ H 2 O 2 ] 0 ) e - k loss , H 2 O 2 t } (5)

Time and concentration data for each pair of samples (one unspiked, one spiked with up to 1 mM H2O2) were fitted to equation 5 using the Microsoft Excel solver function. Fitting parameters were global P′H2O2 and k′loss,H2O2 values, and [H2O2]0 for each sample. For most organisms, three or more replicate measurements (i.e., using three, or more, pairs of spiked/unspiked samples) were performed on each bacterial culture.

Cell-normalized production rates, PH2O2, were then calculated with units of amol cell–1 hr–1 by dividing P′H2O2 by the estimated cell count in each syringe (calculated by multiplying cell density in cell mL–1 by the volume in mL). Normalized decay rate coefficients kH2O2,cell, with units of hr–1 (cell mL–1), were calculated by dividing k′loss,H2O2 by cell density. The difference in normalization stems from the assumptions that are made about production and decay: namely, that production is proportional to the number of cells present, while the rate of [H2O2] loss in mol L–1 hr=1 is proportional to the cell density, [cells] as in Cooper et al. (1994):

rate of H 2 O 2 loss = k H2O2 , cell [ H 2 O 2 ] [ cells ] (6)

Spiked Batch Incubations With Supernatant

5.00 mL aliquots of each bacterial culture were centrifuged as in section “Measurement of H2O2 Production and Decay Rates by Spiked Batch Incubations.” Instead of being discarded, the supernatant was loaded into a syringe and diluted to 50 mL. For each bacterial strain, three pairs of syringes were prepared in this fashion and analyzed by the spiked-batch incubation method. Because there were presumably no cells present in the supernatant, the production and decay data are normalized to the number of cells that originally grew in the medium for comparison purposes.

Incubations with cells were conducted in parallel to incubations of supernatant. After the cultures were centrifuged and the supernatant was removed as described in the previous paragraph, the cells were resuspended in assay medium and centrifuged a second time. The supernatant was removed again, and the cells were resuspended in assay medium before being loaded into a second syringe. The purpose of this additional washing, which was not performed in the other SBI experiments, was to remove all traces of growth medium from the cells.

Conversion Between RecH2O2 and k′loss,H2O2

In order to compare H2O2 decay in spiked batch incubations to that in the flow-through method, decay rate coefficients (k′loss,H2O2) were converted into recoveries (RecH2O2) and vice versa by assuming that the dead volume in the filter (V, in L) was a well-mixed reactor at steady state (details in Supplementary Material of Schneider et al., 2016). This leads to the equation:

k l o s s , H 2 O 2 = ( Q V ) { 1 Rec H 2 O 2 - 1 } (7)

which can also be rearranged to give:

Rec H 2 O 2 = ( Q V ) k l o s s , H 2 O 2 + Q V (8)

Calculation of Detection Limit for H2O2 Production

The detection limit for P′H2O2 in spiked batch incubations can be estimated by realizing that as steady state is approached, the exponential term of equation 5 approaches zero. Thus the steady state concentration of H2O2 is:

[ H 2 O 2 ] s s = P H 2 O 2 k l o s s , H 2 O 2 (9)

Early data in a spiked batch incubation experiment are most important for determining k′loss,H2O2, but data collected later, as [H2O2] approaches this steady-state value, are needed to adequately constrain the value of P′H2O2. Eq. 9 can therefore be used to estimate the detection limit for P′H2O2, DLprod, in the spiked batch incubation method:

DL prod = DL [ H 2 O 2 ] k loss , H 2 O 2 (10)

where DL[H2O2] is the detection limit for [H2O2]. Thus, the detection limit for P′H2O2 is a function of k′loss,H2O2 for each species. Dividing by cell density then provides a cell-normalized detection limit of production.

Replicate measurements of [H2O2] at moderate concentrations (∼30 nM) can be made with a typical standard deviation of less than 1 nM; however, near the detection limit of the acridinium ester method, [H2O2] can be determined, at best, with a standard deviation of about 3 nM. We therefore estimate DL[H2O2] as 10 nM for spiked batch incubations.

Estimation of DLprod for the flow-through method was obtained via sensitivity analysis. For each organism, we took a representative data set and adjusted [H2O2]unspiked,cells by 3 nM while holding values for [H2O2]unspiked,direct, [H2O2]spiked,cells, and [H2O2]spiked,direct constant. The change in PH2O2,cell from the original value was set as DLprod for that organism.

For both of these methods, detection limits were estimated rather than directly measured. As a result, we still report the numerical value of measurement less than an order of magnitude below these detection limits. Such measurements should be assumed to have a high associated uncertainty. We ascribed any measurement more than an order of magnitude below the detection limit to methodological noise, and report those measurements as zero.

Replicates and Measurement Uncertainties

Statistical significance for all results was assessed using a two-tailed t-test with the minimum level for significance at p = 0.05. Reported uncertainties in figures and text represent one standard deviation.

Results and Discussion

H2O2 Decay and Recovery Rates

The eight bacterial strains studied by the flow-through method exhibited a wide range of recovery percentages, ranging from 9 ± 6% (Vibrio sp. A535) to 107 ± 5% (Marinobacter sp. AzsJAc-4) (Table 2 and Figure 1). Conversions yielded decay rate coefficients ranging from 4.0 ± 0.6 × 10–8 hr–1 (Sulfitobacter sp. EE-36) to 5.2 ± 2.9 × 10–6 hr–1 (Vibrio sp. A535) (Table 2). A decay rate coefficient could not be calculated for Marinobacter sp. AzsJAC-4 because of its recovery percentage greater than 100% (Table 2).

TABLE 2
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Table 2. Calculated values for hydrogen peroxide recoveries (RecH2O2) and normalized decay rate coefficient kH2O2,cell for both spiked batch incubation (SBI) and flow-through (FT) methods for SBI.

FIGURE 1
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Figure 1. Recovery percentages for bacterial strains evaluated with both spiked batch incubations (green bars) and flow-through method (blue bars). Uncertainties represent the standard deviation.

Decay rate coefficients determined by spiked batch incubations ranged from 2.2 ± 0.2 × 10–8 hr–1 (cell mL–1)–1 for Tenacibaculum sp. UAzPsLept-5 to 2.0 ± 0.1 × 10–6 hr–1 (cell mL–1)–1 for Vibrio sp. A535. Decay rate coefficients were converted into recovery percentages for comparison purposes and method validation. For each culture evaluated by both flow-through and spiked incubation, there was good agreement between recovery values (two-tailed t-test, p > 0.05) for five of the eight organisms, with the exceptions being Halomonas sp. VMMm1-3c, Marinobacter sp. AzsJAC-4 and S. oneidensis sp. MR-1 (Table 2 and Figure 1).

Only one previous study to our knowledge quantified kH2O2,cell for bacterial cultures: Cooper et al. (1994) found kH2O2,cell to be 1.4 × 10–7 hr–1 (cells mL–1)–1 for Vibrio alginolyticus and 3.1 × 10–7 hr–1 (cells mL–1) –1 for E. cloacae. A value for kH2O2,cell can be inferred for V. pelagius in Petasne and Zika (1997) by finding the half-life of H2O2 in their Figure 5; this gives a value of 9 × 10–8 hr–1 (cells mL–1)–1. Although these figures are an order of magnitude lower than the kH2O2, cell for Vibrio sp. A535, which was found here to be 2.05 ± 0.22 × 10–6 hr–1 (cells mL–1)–1, they are the same order of magnitude as kH2O2,cell for several of the bacterial species in this study.

Decay rate coefficients for the strains studied varied by up to two orders of magnitude. Since decay has previously been linked to cell-surface processes (Moffett and Zafiriou, 1990), we examined the idea that larger decay rates were linked to larger cell surface area. We normalized raw decay rate coefficients (k′H2O2) by total cell surface area and compared these to the previously calculated cell density-normalized decay rate coefficients. The surface-normalized decay rate coefficients also showed a variation of approximately two orders of magnitude (Supplementary Figure S1). Thus, there must be a factor other than cell-surface processes that affect H2O2 decomposition.

We also performed spiked batch incubations of supernatant from two bacterial strains (R. pomeroyi sp. DSS-3 and Paracoccus sp. HIJAc-3c). The raw (non-normalized) decay rate constants for these experiments were 1.2 ± 0.2 hr–1 for R. pomeroyi sp. DSS-3 and 1.9 ± 0.3 hr–1 for Paracoccus sp. HIJAc-3c. For both strains, H2O2 incubations of the supernatant showed decay that was of a similar magnitude as that of the corresponding cells (Figure 2A). These supernatant experiments also indicate that decay may occur by at least two pathways – one (or more) pathways involving cell-surface or intracellular mechanisms, and one (or more) pathways involving secreted soluble enzymes or small molecules. However, we cannot rule out that components originally present in the growth medium contributed to the decay measured in supernatant. It should be emphasized that compounds present in supernatant could not have contributed to measurements in which cells were present (data shown in Figure 1, Table 2, and green bars in Figure 2), since these were conducted on cells resuspended in assay medium. Additionally, cell incubations used as comparisons for the supernatant experiments were rinsed to remove all traces of assay medium; these showed decay rates similar to incubations with unrinsed cells. Control experiments with only artificial seawater showed decay rate coefficients of 0 ± 0 hr–1.

FIGURE 2
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Figure 2. Comparison of (A) decay rate coefficients and (B) production rates for cells and supernatant in cultures of R. pomeroyi sp. DSS-3 and Paracoccus sp. HIJAc-3c. Production and decay data in the supernatant are normalized to the number of cells originally grown in that medium for comparison purposes.

Observations of natural water samples corroborate our suggestion that H2O2 decay may be linked to both cell-surface processes and extracellular enzymatic activity, are corroborated by. Previous studies have shown that filtering greatly reduces, but does not completely eliminate, decomposition of H2O2. For example, Cooper et al. (1994) showed an increase in half-life from 19.1 h for 1 μm-filtered lake water to 58.1 h for 0.2 μm-filtered lake water, while Yuan and Shiller (2001) observed a decay-rate constant for 0.2 μm-filtered seawater that was half that of unfiltered water. H2O2 decay has therefore been strongly linked to microorganisms in natural waters. However, both studies, as well as a subsequent study (Roe et al., 2016) showed non-zero decay rate constants in filtered water. Observations of H2O2 decay in ultra-filtered water led Yuan and Shiller (2001) to attribute some decay in unfiltered seawater to colloidal particles. By contrast, autoclaving completely stopped all H2O2 decay in coastal seawater (Petasne and Zika, 1997). Since autoclaving would destroy enzymatic activity, this finding, along with the results of the supernatant incubations in the current study, suggests that H2O2 decomposition in filtered water is likely dominantly enzymatic.

H2O2 Production Rates

For eight of the bacterial strains studied, H2O2 production rates were determined by two methods, flow-through and spiked batch incubation, while the remaining four strains were examined only by spiked batch incubation.

Of the eight bacterial strains examined by the flow-through method, four (Vibrio sp. A535, S. oneidensis sp. MR-1, Shewanella sp. ANA-3, and Halomonas sp. HIJAc-3c) had all three measurements of PH2O2 above the estimated detection limit (blue bars in Figure 3), with average PH2O2 values of 307 ± 207, 2.38 ± 1.40, 0.88 ± 0.53, and 0.78 ± 0.15 amol cell–1 hr–1, respectively. Although all measurements were above the detection limit, variation between individual production measurements was great enough that only Halomonas sp. VMM1-3c had an average production rate that was significantly different from zero (one-tailed t-test, p > 0.05). Of the remaining four bacterial strains evaluated, only Sulfitobacter sp. EE-36 had any measurements above the detection limit.

FIGURE 3
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Figure 3. Individual values for H2O2 production rates by spiked batch incubation (green bars) and flow-through method (blue bars). Vertical black lines indicate detection limit (DLprod) for both methods. Species marked by an asterisk(*) were not evaluated by flow-through methodology. Small circles along y-axis indicate a measurement of zero; dashes (-) along y-axis indicate observed negative production in the flow-through method.

Individual measurements of H2O2 production above our estimated detection limit were also observed in the spiked batch incubations, though less consistently than for the flow-through measurements (green bars in Figure 3). Of the twelve bacterial strains evaluated, only Sulfitobacter sp. EE-36 had all individual production rate measurements over the detection limit. This strain also had an average value for PH2O2 (0.75 ± 0.37) that was significantly different from zero. Seven species (Halomonas sp. VMMm1-3c, Marinobacter sp. AzsJAc-4, Paracoccus sp. HIJAc-3c, R. pomeroyi sp. DSS-3, S. oneidensis sp. MR-1, Sulfitobacter sp. EE-36, and Tenacibaculum sp. UAzPsLept-5) met the relatively low criterion of having half or more of their individual production measurements above the detection limit. For these species, average values for PH2O2 were 0.59 ± 0.54, 4.67 ± 4.85, 1.05 ± 1.37, 0.15 ± 0.16, 0.34 ± 0.30, 0.75 ± 0.37, and 0.10 ± 0.14 amol cell–1 hr–1, respectively. Of the remaining five bacterial strains, three (Vibrio sp. A535, Bacillus sp. AzsLept-1c, and Erythrobacter sp. SD-21) had no measurements over the detection limit, while the remaining two strains (A. manganoxydans sp. SI85-9A1 and Shewanella sp. ANA-3) had fewer than half of the measurements over the detection limit.

Measurements of PH2O2 for supernatant were also obtained and compared to those of cells taken from the supernatant during the incubations described in the previous section (Figure 2). In the two bacterial culture supernatants thus evaluated, raw (non-normalized) production rates ranged between 0 and 13 nM hr–1 for R. pomeroyi sp. DSS-3 and 0 and 31 nM hr–1 for Paracoccus sp. HIJAc-3c; control experiments in artificial seawater exhibited production rates between 0 and 0.3 nM hr–1. When normalized to the number of cells originally grown in the cultures, Paracoccus sp. HIJAc-3c and R. pomeroyi sp. DSS-3, PH2O2 measurements for growth medium were of a similar magnitude to those of the cells (Figure 2B). Production of H2O2 in supernatant could be attributed to enzymes or other exuded labile, redox-active compounds (LRACs) (Zinser, 2018b).

As discussed for decay above, components originally present in the growth medium could have contributed to the production rates measured in the two supernatant experiments. Morris and Zinser (2013) showed that H2O2 production could occur by exposing zwitterionic buffers such as those used in growth media to light. However, the bacteria used in this experiment were grown in a dark incubator, and syringes used for spiked batch incubations were covered between time points. Given the limited light exposure, it is unlikely that H2O2 production in the supernatant is due to light-buffer interactions. Furthermore, the growth medium in question was K medium (Andersened., 2005) which contains Tris buffer; Morris and Zinser (2013) found that Tris buffer produced considerably less H2O2 than buffers such as HEPES. While we cannot rule out that other compounds in the growth medium contributed to dark H2O2 production measured in supernatant (blue bars in Figure 2), they could not have contributed to the production rates measured in the presence of cells (green bars in Figure 2 and all other measurements presented in this work.) We conclude that observed measurable production in both bacterial cultures and supernatant suggest that both LRACs and cell processes, either inside the cell or on its surface, contribute to PH2O2.

Measurement Variability and Comparison Between Spiked Batch Incubation and Flow-Through Methods

Both methods for measuring PH2O2 demonstrate high variability. A natural question to ask is whether the fluctuations are due to method limitations or whether the measurements reflect real differences in the behavior of the organisms, for example due to changes in extracellular conditions.

High variability would be expected when measurements were taken close to the calculated detection limit. This would especially be true for the flow-through method, where six of the eight species examined had PH2O2 measurements less than an order of magnitude above the detection limit. Spiked batch incubations had lower detection limits, with eight of the strains showing some measurements more than an order of magnitude above detection limit. Yet the variability in PH2O2 measurements was higher overall in spiked batch incubations – the standard deviation of the PH2O2 measurements was greater than the average PH2O2 measurement for 8 out of 12 strains in spiked batch incubations, as opposed to 2 out of 5 for flow-through. Thus, the variability is not clearly linked to measuring PH2O2 close to the detection limit.

The observation that, for many of the organisms examined, spiked batch incubation measurements were either well below the detection limit (measurements indicated by a circle along the y-axis in Figure 3) or well above suggests the possibility that bacteria exist in two states: one in which they produce H2O2 and one in which they do not. This observation applies to eight of the twelve species assessed by spiked-batch incubation – A. manganoxydans sp. SI85-9A1, Halomonas sp. VMMm1-3c, Marinobacter sp. AzsJAc-4, Paracoccus sp. HIJAc-3c, R. pomeroyi sp. DSS-3, Shewanella sp. ANA-3, S. oneidensis sp. MR-1, and Tenacibaculum sp. UAzPsLept-5. For Halomonas sp. VMMm1-3c, Paracoccus sp. HIJAc-3c, R. pomeroyi sp. DSS-3 and Shewanella sp. ANA-3, the ranges of non-zero PH2O2 values measured by SBI overlaps with the ranges measured by the flow-through method. This overlap could indicate that the range of non-zero PH2O2 measured by either method indicates the strain’s H2O2 production while in the “on” mode. However, both for R. pomeroyi sp. DSS-3 and for Paracoccus sp. HIJAc-3c, the flow-through measurements of PH2O2 were below our estimated detection limit for that technique, and also included negative PH2O2 measurements (discussed more below), and therefore should be interpreted with caution. It is unclear why replicates grown from the same freezer stocks and, in most cases, sampled from the same liquid culture would inconsistently “turn on” hydrogen peroxide production. It appears that subtle differences in the environment and handling of the cells can affect the production rate of hydrogen peroxide.

For one bacterial strain, the increased flow rates of the flow-through method may be the “switch” that turns on H2O2 production. Vibrio sp. A535 had PH2O2 values of zero for all of the spiked-batch incubations but, for flow-through measurements, had the highest observed PH2O2 values observed in this study. S. oneidensis sp. MR-1 showed a less extreme version of this behavior, with H2O2 production almost an order of magnitude higher in flow-through than in spiked-batch incubations.

An increase in H2O2 production with increasing flow rates has been observed in previous studies of marine algae. We observed that the flow rate used to load diatoms on a filter affected H2O2 production by T. weissflogii (Schneider et al., 2016). The stress induced by loading cells on the filter by syringe (approximate flow rate 5 mL min–1) induced measured values of PH2O2,cell of 800 amol cell–1 hr–1, while cells loaded onto a filter by peristaltic pump (flow rate 0.6 mL min–1) had PH2O2 indistinguishable from zero. By contrast, T. oceanica had similar values of PH2O2 under both conditions. In another study, Shaked and Armoza-Zvuloni (2013) observed a higher release of H2O2 from coral with faster stirring. While they attributed this to increased transport of H2O2 from the coral to surrounding waters, high stirring speed could also have caused an increase in microbial production of H2O2, for example by the microbes in the external mucous layer of the coral. In any case, it is plausible that, analogously to our previous findings for diatoms, higher flow rates cause increased ROS production in some bacterial strains but not in others. Spiked batch incubations would be expected to have lower values of PH2O2 than the flow-through method for those organisms in which flow-related stress affect ROS production.

In contrast, one organism, Sulfitobacter sp. EE-36 seems to have lower PH2O2 values in flow-through than in spiked batch incubation. What could explain this? As mentioned in section “H2O2 Production Rates,” some organisms are likely to produce at least part of their H2O2 by exuding enzymes into their environment. In the two strains whose exudates we studied – R. pomeroyi sp. DSS-3 and Paracoccus sp. HIJAc-3c – the cell-surface processes seemed about equal to those produced by exuded enzymes. However, different bacterial strains may produce different proportions of their H2O2 via exuded enzymes. In the flow-through method, these enzymes would be continuously washed away by the assay medium; thus, the effect flow has on PH2O2 may depend considerably from species to species. Unfortunately, due to time constraints, we were unable to examine supernatant for all bacterial strains and can therefore only speculate exactly how different strains might respond to flow conditions.

Three species, Paracoccus sp. HIJAc-3c, R. pomeroyi sp. DSS-3 and Marinobacter sp. AzsJAc-4, had negative measurements of H2O2 production by the flow-through method (Supplementary Table S1 and Supplementary Figure S2). For two of these, Paracoccus sp. HIJAc-3c ,R. pomeroyi sp. DSS-3, the negative values were small and only appeared in some replicates, and could be accounted for by method uncertainty. However, in the case of Marinobacter sp. AzsJAc-4, the negative production rates were consistent and substantial. Since flow-through results accounted for decay and should never yield production rates below zero, this result implies that at least one of our assumptions was not true – most likely, the assumption that decay was first-order with respect to H2O2. If production was low or non-existent, and if the decay rate was less than proportional to [H2O2] (e.g., Michaelis-Menten kinetics), we would expect to see a much smaller drop between [H2O2]spiked,direct and [H2O2]spiked,cells than between [H2O2]unspiked,direct and [H2O2]unspiked,cells. In fact, this is what was observed in the case of Marinobacter sp. AzsJAc-4 (Supplementary Figure S3).

H2O2 Production Compared to O2 Production

Since dismutation of O2 produces H2O2 in a 2:1 ratio, comparing PH2O2,cell with superoxide production (PO2–,cell) allows an evaluation of O2 dismutation as a possible production pathway for H2O2. Given high expected variability, average values for PH2O2 are not necessarily the best way to express what may be occurring with a particular organism. We have therefore chosen to represent PH2O2 graphically as a range of production rates, and compare this to the range of values for PO2–,cell determined by Diaz et al. (2013) (Figure 4).

FIGURE 4
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Figure 4. Comparison of non-zero values for PH2O2,cell (green – spiked batch incubation; blue – flow through) with PO2–,cell (red). Along the y-axis, red text indicates a species that produces more O2 than H2O2, while blue text indicates higher production of H2O2 than of O2. A pound (#) adjacent to the name indicates a species only evaluated by spiked batch incubation; @ indicates no non-zero PH2O2 values were observed for spiked batch incubations; while a double dagger (‡) indicates that negative production was observed for at least some values in the flow-through method.

Of the twelve species studied, nine (A. manganoxydans sp. SI85-9A1, Erythrobacter sp. SD-21, Halomonas sp. VMM1-3c ,Marinobacter sp. AzsJAC-4Paracoccus sp. HIJAc-3c ,R. pomeroyi sp. DSS-3, Shewanella sp. ANA-3, Sulfitobacter sp. EE-36, and Tenacibaculum sp. UAzPsLept-5; black font in Figure 4) have a range of PH2O2,cell of comparable magnitude as PO2–,cell (that is, the ranges differ by less than an order of magnitude). Here, PH2O2,cell is not inconsistent with a 2:1 PO2–,cell:PH2O2,cell ratio, although a more specific comparison is not available due to the high levels of variability in the measurements. Bacillus sp. AzsLept-1c has measurable production of O2 but a PH2O2,cell value that is below detection; thus, it produces considerably more O2 than H2O2. In this species, small amounts of H2O2 might be produced through the O2 dismutation pathway, but O2 may also be lost to processes other than dismutation. S. oneidensis sp. MR-1 had a range of measured PH2O2,cell values that were substantially higher than PO2–,cell. While conflicting results between the flow-through and spiked batch incubation methods make a comparison for Vibrio sp. A535 difficult, the flow-through value for PH2O2,cell (which represents conditions closer to those under which the PO2–,cell measurements were made) is two orders of magnitude higher than PO2–,cell. Thus, for Vibrio sp. A535 and S. oneidensis sp. MR-1, it is possible that H2O2 is produced, at least in part, via biological pathways that do not involve O2 production.

The variety in PO2–,cell:PH2O2,cell ratios is similar to that observed in diatoms of genus Thalassiosira (Schneider et al., 2016) and in field studies of freshwater and brackish ponds (Zhang et al., 2016b). In the former study, T. oceanica was found to have the 2:1 PO2–,cell:PH2O2,cell ratio indicative of production of H2O2 through dismutation, T. pseudonana produced considerably more H2O2 than O2, and T. weissflogii produced considerably less H2O2 than O2. Organisms producing more H2O2 than O2 have been observed in other studies; for example, H. carterae was shown to produce H2O2 but not O2 (Palenik et al., 1987). Likewise, Zhang et al. (2016b) observed decoupling of O2 and H2O2 production rates in samples taken from freshwater and brackish ponds, with samples showing PO2–,cell:PH2O2,cell ratios both below and above the 2:1 ratio that would indicate O2 undergoing dismutation to H2O2.

As mentioned previously, the flow rate used to load diatoms on the filter affected H2O2 production by T. weissflogii (Schneider et al., 2016). However, we have not previously observed changes in extracellular superoxide production as a function of flow rate, suggesting a decoupling of this response, perhaps because the increased H2O2 is due to intracellular release. For methodological reasons, PH2O2,cell and PO2–,cell were evaluated at different flow rates – 0.6 mL min–1 for H2O2 and 2.0 mL min–1 for O2. This may add to uncertainty in the PO2–,cell:PH2O2,cell ratio in flow-through numbers.

Application of Findings to Natural Water Systems

Bacterially mediated decay of H2O2 in natural water systems was estimated by assuming a total bacterial abundance of 106 cells mL–1 in coastal waters and freshwater and 105 cells mL–1 in the oligotrophic ocean using the decay rate from R. pomeroyi sp. DSS-3 as a typical (near median) decay rate found in this study. The estimated bacterial H2O2 decay rate coefficient in the oligotrophic ocean is 0.007 hr–1, which is considerable in comparison to observed overall values of 0.003 to 0.011 hr–1 in the oligotrophic ocean (Petasne and Zika, 1997; Yuan and Shiller, 2001, 2005; AveryJr., Cooper et al., 2005).

In coastal marine and freshwater systems, bacteria also may make a substantial contribution to H2O2 decay. Estimated bacterial decay rate coefficients would be approximately 0.066 hr–1 which would comprise a substantial fraction of the 0.006 to 0.28 hr–1 decay rate coefficient measured in coastal waters (Vermilyea et al., 2010b and references cited therein) or the 0.32 to 0.09 hr–1 decay rate coefficients calculated from measured H2O2 half-lives in estuarine Chesapeake Bay (Cooper et al., 1994). Freshwaters, which exhibit a wider range of decay rates—observed decay rate coefficients range between 0.11–8.9 hr–1 (Cooper et al., 1994; Dixon et al., 2013; Marsico et al., 2015)—could potentially have high bacterial contributions to decay, but more likely it comprises a small percentage of the total. The latter finding corresponds with the findings of Marsico et al. (2015) that dark production in freshwater is most strongly correlated with algal cell counts, with only a weaker correlation to bacterial cell densities.

When assessing the importance of bacteria to regulation of H2O2 in natural waters, it is important to consider the wider context of the effects of H2O2 on a microbial community. Reactive oxygen species are likely used by a variety of organisms in natural water systems for purposes such as signaling, allelopathy, and growth (Oda et al., 1995; Diaz and Plummer, 2018). At the same time, high H2O2 levels have been shown to have deleterious effects on aquatic microbial communities, including reduced growth in some bacterial populations (Weinbauer and Suttle, 1999; Morris et al., 2011). This has been attributed to adverse effects on glucose incorporation and respiration processes in bacteria (Santos et al., 2012) caused by the impact of H2O2 on extracellular enzymatic activity (Baltar et al., 2013). Thus, it is necessary for aquatic microbial communities to maintain balanced exogenous H2O2 levels – low enough that important community members are not damaged but high enough that they can function.

However, the burden of decomposing H2O2 is not borne equally by all community members, as shown both previously and within this study. Four of the bacterial strains (Bacillus sp. AzsLept-1c ,Halomonas sp. VMM1-3c, Marinobacter sp. AzsJAC-4, and Tenacibaculum sp. UAzPsLept-5) within this particular study were isolated from benthic sediments in the same estuary (Elkhorn Slough), yet show decay rate coefficients that vary by up to two orders of magnitude (Table 2). Planktonic marine bacteria (e.g., R. pomeroyi sp. DSS-3 and Vibrio sp. A535) also show a similar range of decay rates. These results correlate with what has been found in previous studies: the cyanobacterium Prochlorococcus (Morris et al., 2011) and some strains of the similar bacterium Synechococcus (Zinser, 2018a) are completely dependent upon other microbes to scavenge H2O2. If known helper bacterial strains, such as Alteromonas, were examined in future studies, we can speculate that they would fall at the higher end of the range of decay rates. However, given that the ability of a particular species to degrade H2O2 may not expressed within a particular community (Morris et al., 2016), it is difficult to predict which bacterial strain might contribute most to H2O2 decay. Nonetheless, it is clear that bacteria have the potential to be major players in regulating H2O2 levels in natural water systems.

The same methodology used to estimate bacterial contributions to H2O2 decay can also be used to approximate dark biological production of H2O2 in natural water systems, again using R. pomeroyi as a near-median model organism. Given the uncertainties associated with PH2O2 measurements and differences of several orders of magnitude in production rates between planktonic marine bacterial species, these should be considered as order-of-magnitude approximations only. We compare these estimated production rates to studies in which gross (rather than net) values of PH2O2 were determined, since the cell-normalized production rates in this study are also calculated by accounting for effects of decay on gross production rates.

Using the median value for PH2O2,cell and 105 cells mL–1, bacteria might contribute 0.15 nM hr–1 to dark production rates of 0.2 to 3.0 nM hr–1 (Roe et al., 2016) in the oligotrophic ocean. Coastal waters would have an estimated bacterial contribution of 1.5 nM hr–1, a substantial fraction of observed gross production rates of 0.8–4.0 nM hr–1 (Moffett and Zafiriou, 1990; Vermilyea et al., 2010b). However, the similar rate of 1.5 nM hr–1 might be only a tiny fraction of the observed gross dark PH2O2 in freshwater, 20–200 nM hr–1 in non-oligotrophic freshwaters (Vermilyea et al., 2010b; Marsico et al., 2015). Again, this corresponds with the findings of Marsico et al. (2015) which show no correlation between bacterial abundance and PH2O2.

Future Work

While the current study advances the existing understanding of bacterial effects of H2O2 dynamics in natural water systems, in many ways it creates more questions than it answers. First, it reinforces what previous studies have indicated: namely, that H2O2 and O2 are created through multiple pathways that may not be coupled to each other. These pathways may be associated with cell-surface processes or with labile redox-active compounds (LRACs) released into the environment. Additional research is needed to determine which processes might be responsible for bacterial production of H2O2 in the strains studied. In particular, further studies of supernatant may help elucidate not only which strains produce LRACs, but also what substances might be catalyzing H2O2 production and decay. With a better understanding of these pathways, genomics and metatranscriptomics might be used to more easily identify which additional strains might be major contributors to H2O2 production in natural water systems.

Data Availability Statement

All datasets generated for this study are included in the article/Supplementary Material.

Author Contributions

RB, CH, and BV conceived and planned the experiments, and contributed to interpretation of the results. RB carried out the experiments and took the lead in writing the manuscript. BV supervised the project. All authors provided critical feedback and helped to shape the research, analysis, and manuscript.

Funding

This research was supported by NSF grant OCE-1131734/1246174 to BV and CH.

Conflict of Interest

The authors declare that the research was conducted in the absence of any commercial or financial relationships that could be construed as a potential conflict of interest.

Supplementary Material

The Supplementary Material for this article can be found online at: https://www.frontiersin.org/articles/10.3389/fmars.2020.00072/full#supplementary-material

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Keywords: reactive oxygen species, hydrogen peroxide, heterotrophic bacteria, H2O2 production, H2O2 decomposition

Citation: Bond RJ, Hansel CM and Voelker BM (2020) Heterotrophic Bacteria Exhibit a Wide Range of Rates of Extracellular Production and Decay of Hydrogen Peroxide. Front. Mar. Sci. 7:72. doi: 10.3389/fmars.2020.00072

Received: 21 October 2019; Accepted: 30 January 2020;
Published: 18 February 2020.

Edited by:

Mark James Hopwood, GEOMAR Helmholtz Centre for Ocean Research Kiel, Germany

Reviewed by:

Surabhi Mishra, University of Florida, United States
Erik Zinser, The University of Tennessee, Knoxville, United States

Copyright © 2020 Bond, Hansel and Voelker. This is an open-access article distributed under the terms of the Creative Commons Attribution License (CC BY). The use, distribution or reproduction in other forums is permitted, provided the original author(s) and the copyright owner(s) are credited and that the original publication in this journal is cited, in accordance with accepted academic practice. No use, distribution or reproduction is permitted which does not comply with these terms.

*Correspondence: Robin J. Bond, bondr@evergreen.edu