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Accepted Manuscript Title: Oxidation of elemental sulfur, tetrathionate and ferrous iron by the psychrotolerant Acidithiobacillus strain SS3 Authors: Daniel Kupka, Maria Liljeqvist, Pauliina Nurmi, Jaakko A. Puhakka, Olli H. Tuovinen, Mark Dopson PII: S0923-2508(09)00159-4 DOI: 10.1016/j.resmic.2009.08.022 Reference: RESMIC 2788 To appear in: Research in Microbiologoy Received Date: 20 May 2009 Revised Date: 19 August 2009 Accepted Date: 25 August 2009 Please cite this article as: D. Kupka, M. Liljeqvist, P. Nurmi, J.A. Puhakka, O.H. Tuovinen, M. Dopson. Oxidation of elemental sulfur, tetrathionate and ferrous iron by the psychrotolerant Acidithiobacillus strain SS3, Research in Microbiologoy (2009), doi: 10.1016/j.resmic.2009.08.022 This is a PDF file of an unedited manuscript that has been accepted for publication. As a service to our customers we are providing this early version of the manuscript. The manuscript will undergo copyediting, typesetting, and review of the resulting proof before it is published in its final form. Please note that during the production process errors may be discovered which could affect the content, and all legal disclaimers that apply to the journal pertain.

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Page 1: Accepted Manuscript

Accepted Manuscript

Title: Oxidation of elemental sulfur, tetrathionate and ferrous iron by thepsychrotolerant Acidithiobacillus strain SS3

Authors: Daniel Kupka, Maria Liljeqvist, Pauliina Nurmi, Jaakko A. Puhakka, Olli H.Tuovinen, Mark Dopson

PII: S0923-2508(09)00159-4

DOI: 10.1016/j.resmic.2009.08.022

Reference: RESMIC 2788

To appear in: Research in Microbiologoy

Received Date: 20 May 2009

Revised Date: 19 August 2009

Accepted Date: 25 August 2009

Please cite this article as: D. Kupka, M. Liljeqvist, P. Nurmi, J.A. Puhakka, O.H. Tuovinen, M. Dopson.Oxidation of elemental sulfur, tetrathionate and ferrous iron by the psychrotolerant Acidithiobacillusstrain SS3, Research in Microbiologoy (2009), doi: 10.1016/j.resmic.2009.08.022

This is a PDF file of an unedited manuscript that has been accepted for publication. As a service toour customers we are providing this early version of the manuscript. The manuscript will undergocopyediting, typesetting, and review of the resulting proof before it is published in its final form. Pleasenote that during the production process errors may be discovered which could affect the content, and alllegal disclaimers that apply to the journal pertain.

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For publication 1

Oxidation of elemental sulfur, tetrathionate and ferrous iron by the 2

psychrotolerant Acidithiobacillus strain SS3 3

4

Daniel Kupka,a Maria Liljeqvist,b Pauliina Nurmi,c,1 Jaakko A. Puhakka,d Olli H. Tuovinenc,d 5

Mark Dopsonb,* 6

7

aInstitute of Geotechnics, Slovak Academy of Sciences, Watsonova 45, SK-043 53 Košice, Slovakia 8

bDepartment of Molecular Biology, Umeå University, SE-901 87 Umeå, Sweden cDepartment of 9

Chemistry and Bioengineering, Tampere University of Technology, P.O. Box 541, FI-33101 Tampere, 10

Finland 11

dDepartment of Microbiology, Ohio State University, 484 West 12th Avenue, Columbus, Ohio 43210, 12

USA 13

Received 20 May 2009; accepted 25 August 2009 14

Email addresses: Daniel Kupka ([email protected]), Maria Liljeqvist ([email protected]), Pauliina Nurmi 15

([email protected]), Jaakko A. Puhakka ([email protected]), Olli H. Tuovinen ([email protected]), Mark 16

Dopson ([email protected])*Correspondence and reprints 17

18 1Present address: MTT Agrifood Research Finland, Biotechnology and Food Research, FI-31600 Jokioinen, Finland. 19

20

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Abstract 21

22

Mesophilic iron and sulfur-oxidizing acidophiles are readily found in acid mine drainage 23

sites and bioleaching operations, but relatively little is known about their activities at 24

suboptimal temperatures and in cold environments. The purpose of this work was to 25

characterize the oxidation of elemental sulfur (S0), tetrathionate (S4O62-) and ferrous iron 26

(Fe2+) by the psychrotolerant Acidithiobacillus strain SS3. The rates of elemental sulfur and 27

tetrathionate oxidation had temperature optima of 20° and 25°C, respectively, determined 28

using a temperature gradient incubator that involved narrow (1.1°C) incremental increases 29

from 5° to 36°C. Activation energies calculated from the Arrhenius plots were 61 and 89 kJ 30

mol-1 for tetrathionate and 110 kJ mol-1 for S0 oxidation. The oxidation of elemental sulfur 31

produced sulfuric acid at 5°C and decreased the pH to approximately 1. The low pH inhibited 32

further oxidation of the substrate. In media with both S0 and Fe2+, oxidation of elemental 33

sulfur did not commence until all available ferrous iron was oxidized. These data on 34

sequential oxidation of the two substrates are in keeping with upregulation and 35

downregulation of several proteins previously noted in the literature. Ferric iron was reduced 36

to Fe2+ in parallel with elemental sulfur oxidation, indicating the presence of a sulfur:ferric 37

iron reductase system in this bacterium. 38

39

Keywords Acidithiobacillus strain SS3; Iron oxidation; Psychrotolerant; Redox coupling; 40

Qulfur oxidation; Temperature dependency 41

42

43

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1. Introduction 44

45

Bioleaching processes utilize acidophilic Fe2+ and elemental sulfur (S0) oxidizing 46

microorganisms to aid in the solubilization of metals from sulfide minerals [27, 31]. In 47

bioleaching, the sulfur entity in sulfide minerals is oxidized chemically by Fe3+ or directly by 48

bacteria with oxygen as the electron acceptor. Typical intermediates from these reactions are 49

secondary sulfide minerals (e.g. CuS from CuFeS2), thiosulfate (S2O32-), polythionates 50

(SnO62-), polysulfides (Sn

2-) and elemental sulfur (S0) [34]. These sulfur compounds are 51

further oxidized to sulfate in acid-producing reactions. S0 is biologically oxidized to sulfate in 52

the presence of oxygen according to the net equation [1] (the major sulfate species in acidic 53

solutions is bisulfate (pKa2 1.92)). 54

2S0 + 3O2 + 2H2O → 2HSO4- + 2H+ [1] 55

The use of Fe3+ as an external electron acceptor for Acidithiobacillus ferrooxidans 56

mediated oxidation of elemental sulfur [eqn. 2] under oxic and anoxic conditions has been 57

reported [6, 28, 35]. 58

S0 + 6Fe3+ + 4H2O → HSO4- + 6Fe2+ + 7H+ [2] 59

In bioleaching processes, S0 can precipitate on sulfide mineral surfaces and slow down 60

the diffusion of reactants and products to and from the mineral surface, thereby passivating 61

the surface [22, 33, 42]. The passivating S0 layer may be removed or partially alleviated by 62

sulfur-oxidizing acidophilic bacteria and archaea [9, 11], but oxidation of such sulfur rims is 63

relatively slow. Bioleaching and associated iron oxidation involves acidic sulfate-containing 64

solutions which promote the precipitation of schwertmannite (eqn. 3) and jarosites such as K-65

jarosite (eqn. 4). 66

8Fe3+ + SO42- + 14H2O Fe8O8(OH)6SO4 + 22H+ [3] 67

3Fe3+ + K+ + 2SO42- + 6H2O KFe3(SO4)2(OH)6 + 6H+ [4] 68

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The chemical and biological oxidation of the S-entity in sulfide minerals is central to 69

metal dissolution, acid consumption or formation, and passivation in biological leaching 70

processes. Understanding of the biological oxidation of inorganic sulfur compounds at low 71

temperatures is therefore requisitely important for management of bioleaching processes and 72

environmental problems with mine waste rocks in boreal environments. Bacterial oxidation 73

of sulfide minerals at low temperatures has been reported [1, 12, 13, 25] and a number of 74

acidophilic iron-oxidizing strains have been isolated that are capable of growth at low 75

temperatures [5, 14]. In our previous work, we characterized growth and iron oxidation of an 76

Acidithiobacillus ferrooxidans strain SS3 at low temperatures [24]. Strain SS3 is 77

psychrotolerant (optimum growth at 20° to 40°C, but also grows at 4°C). The 16S rRNA 78

gene sequence of strain SS3 [24] aligned in a clade with other isolates from boreal 79

environments, including clone T7 from a pilot scale bioheap [29] and strain NO-37 from an 80

acid mine drainage site [19]. In this study, we have investigated the oxidation of S0 and 81

tetrathionate (S4O62-) by Acidithiobacillus strain SS3 and determined the corresponding 82

activation energy values for the oxidation of these substrates. In addition, redox coupling 83

between Fe3+ and S0 was demonstrated in this work. 84

85

2. Materials and methods 86

87

2.1 Microorganisms and growth conditions 88

89

Acidithiobacillus strain SS3 [24] was used throughout this study. Based on 16S rRNA 90

gene sequence similarity, strain SS3 aligns in a clade with the newly proposed 91

‘Acidithiobacillus ferrivorans’ sp. nov. [16]. Cultures were incubated in mineral salts 92

medium (pH 2.5) that contained (per liter) 3 g (NH4)2SO4, 0.1 g KCl, 0.5 g K2HPO4, 0.5 g 93

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MgSO4·7H2O, and 0.01 g Ca(NO3)2. For routine subcultures, the medium was amended with 94

5 g S0 L-1 (156 mM) and/or 80 mM Fe2+ as energy source. S0 (precipitated) was from 95

Lachema (Brno, Czech Republic; mean diameter of 30 µm and specific surface area of 0.175 96

m2 g-1). 97

98

2.2 Oxidation of tetrathionate and S0 in temperature gradient incubator 99

100

Oxidation rates of tetrathionate and S0 were measured over a temperature range of 5° to 101

30° ± 0.5°C in a temperature gradient incubator (Test Tube Incubator, Terratec®, Australia). 102

The temperature interval was approximately 1.1°C and the oscillation at 35 min-1. The 103

mineral salts medium was adjusted to pH 2.5 with H2SO4 and supplemented with trace 104

element solution [9] and filter-sterilized 5 mM K2S4O6 or 5 g L-1 (156 mM) S0 (autoclaved at 105

105°C for 30 min). The media were inoculated with approximately 1 × 108 cells from a batch 106

culture of Acidithiobacillus strain SS3 previously grown with the respective substrate. Cell 107

numbers were determined by counting 4’-6-diamidino-2-phenylindole stained cells under 108

epifluorescence microscopy. Changes in the tetrathionate concentration [21] and the pH were 109

measured at intervals. The oxidation data were fitted to the Ratkowsky equation according to 110

eqn. 5 [30]. 111

)1()(1 ))((min

maxTTceTTbt

−⋅−⋅−⋅= [5] 112

where T = temperature (°C); Tmin and Tmax = the minimum and the maximum temperature, 113

respectively; b and c = fitting parameters. The parameter time t is derived from the time it 114

takes for half the tetrathionate concentration to be consumed or for the pH to be decreased by 115

half. The greatest value for the square root of 1/t is derived from the optimum temperature 116

(Topt) shown by the inflection in the fitted curve. Chi-square (distribution when the null 117

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hypothesis is true) and R-square (index of correlation) values were calculated with a 95% 118

confidence interval together with the errors for parameters b and c. Microcal Origin 6.0 119

software was used for construction of the Ratkowsky equation with a non-linear regression 120

model. 121

Linearization of the Arrhenius equation (eqn. 6) based on the rates of tetrathionate 122

oxidation and pH decrease between 6° and 18°C was used to calculate the activation energy 123

(Ea). 124

AlnRT

ln +−= aEk [6] 125

where k = rate constant; A = frequency coefficient; Ea = activation energy (J mol-1); R = gas 126

constant; and T = absolute temperature (K). The rate constants for tetrathionate oxidation 127

were calculated from half-life data, the time it takes for half the tetrathionate concentration to 128

be oxidized (T½=0.693/k). The slope of the linear portion of the Arrhenius plot gives the Ea. 129

Similarly, the rate constants for sulfur oxidation were calculated from the corresponding 130

increases in sulfate concentration over time. Since tetrathionate and elemental sulfur 131

oxidation produces sulfuric acid, rate constants were also estimated from time courses of 132

decreases in pH. 133

134

2.3 Oxidation of elemental sulfur and iron 135

136

Elemental S0 (5 g L-1) was added to the mineral salts medium and autoclaved for 30 min 137

at 105ºC. Filter-sterilized ferrous sulfate and ferric sulfate solutions were added as required 138

and the pH was adjusted to 2.5 with either H2SO4 or KOH. The inocula for all experiments 139

were taken from an iron-grown culture of Acidithiobacillus strain SS3 in the late exponential 140

phase at 4°C (specific growth rate ≈ 0.012 h-1). A fraction of Fe2+ and Fe3+ was introduced 141

into each flask with inoculum. Cultures (100 mL) in 250 mL shake flasks were incubated 142

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aerobically at 4°C and at 180 rpm. Samples were removed at intervals for pH, redox, iron 143

and sulfate analysis. Suspended solids were separated by filtration using 0.22 µm Millipore 144

syringe filters. The Fe2+ concentration was determined spectrophotometrically with the o-145

phenanthroline method [17], Fe3+ with UV/Vis spectroscopy at 300 nm [4] and total soluble 146

iron by atomic absorption spectrometry. The sulfate concentration was determined by the 147

BaCl2 nephelometric method [41]. Sulfur oxidation was also monitored by following changes 148

in pH due to acid formation over time using a combined red-rod type pH electrode and PHM 149

210 pH meter (Radiometer Analytical). Subcultures were routinely inoculated into shake 150

flasks containing S0 to ensure that the bacterial culture was active during the long incubation 151

period. Results are presented as averages (number of replicates (n) = 3) ± SD. 152

153

3. Results 154

155

3.1. Temperature dependency of tetrathionate and S0 oxidation 156

157

The temperature dependency of tetrathionate and S0 oxidation by Acidithiobacillus strain 158

SS3 was determined over a range of 5° to 30°C. The lag phases before tetrathionate oxidation 159

was initiated were <12 h and 360 h for 30° and 5°C, respectively (Fig. 1a). The rates of 160

substrate oxidation were dependent on the temperature. From the data fitted to the Ratkowsky 161

equation (eqn. 5), a temperature optimum of 25°C was calculated for tetrathionate oxidation 162

(Fig. 1b). This was consistent with a temperature optimum of 26°C (Fig. 1c) calculated from 163

the corresponding pH decreases. The Ea values for tetrathionate oxidation were calculated on 164

the basis of decreases in the substrate concentration and pH over time. Linearity in the 165

corresponding Arrhenius plots (Fig. 2a,b) was apparent between 6° and 18°C, whereas rate 166

constants below and above these temperatures deviated from the linearity. The Arrhenius 167

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plots yielded Ea values of 61 (R2 = 0.68) and 89 (R2 = 0.90) kJ mol-1 for tetrathionate 168

oxidation and pH decrease, respectively. 169

For S0 oxidation, a pH decrease was first observed after 280 h (~12 days) of incubation 170

at 5°C, whereas it started almost immediately at 25°C. In contrast to tetrathionate oxidation, a 171

lower temperature optimum of 20°C was calculated for S0 oxidation when the data were 172

fitted to the Ratkowsky equation (Fig. 1d). The temperature range for S0 oxidation was larger 173

than for tetrathionate and lacked a distinct temperature optimum peak. The S0 oxidation rate 174

constants between 6° and 18°C also gave a linear plot for lnk versus the reciprocal 175

temperature (Fig. 2c) with an Ea of 110 kJ mol-1 (R2 = 0.89). However, the Arrhenius plot for 176

S0 oxidation based on the decrease in pH did not give a straight line with high probability 177

over the same temperature range (Fig. 2d), casting doubt on the calculated Ea value of 48 kJ 178

mol-1, although the data unequivocally demonstrated a strong association between the 179

oxidation rate and the temperature. The Arrhenius plots in Figs. 2 b-c may also display 180

biphasic linearity, but this possibility was not investigated further. 181

182

3.2. Oxidation of Fe2+ and S0 at 4°C 183

184

Oxidation of 5 g S0 L-1 (156 mM) by Acidithiobacillus strain SS3 at 4°C started after a 185

30-day lag phase upon the first subculture with iron-grown cells (Fig. 3). The medium 186

initially contained 9 mM Fe2+ carried over with the inoculum. During the lag period, the 187

initial 9 mM Fe2+ was completely oxidized, while the sulfate concentration and pH only 188

slightly changed. The oxidation of S0 yielded a linear increase in sulfate formation over time 189

in a semi-log plot (Fig. 3a) and a linear pH decrease due to H2SO4 production (Fig. 3b). Upon 190

approximately 60% S0 oxidation, the linear decrease in the pH reached a prohibitively low 191

value of 1.1 ± 0.1 that inhibited further S0 oxidation. Determination of the sulfur oxidation 192

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rate using the H+ formation rate has been demonstrated [7, 18]. The diprotic H2SO4 193

dissociates in two steps and thus the relationship between the pH and the rate of S0 oxidation 194

changes when the pH approaches the second dissociation constant of H2SO4 (pKa2 = 1.92). 195

The rate constants from these linear regression lines were 0.045 ± 0.0013 d-1 for net sulfate 196

production and 0.043 ± 0.0013 d-1 for pH change. In the absence of Acidithiobacillus strain 197

SS3, the sulfate concentration did not increase (Fig. 3a) and the pH was more or less constant 198

(Fig. 3b). 199

In the next experiment at 4°C, the concentration of Fe2+ was increased from 9 to 67 mM 200

Fe2+ while the initial S0 concentration was 156 mM (5 g L-1). The concentration of Fe3+ 201

increased to a maximum of 67 mM upon the initial Fe2+ oxidation (Fig. 4a), also indicated by 202

the change in color to reddish-orange with time. The first order rate constant estimated from 203

exponential Fe2+ oxidation was 0.012 h-1. This value corresponds to the generation time 58 h 204

(g = ln2/k) and is in agreement with previously observed estimates with Fe2+ alone [24]. 205

Concurrently, the concentration of soluble sulfate decreased, indicating the precipitation of 206

Fe(III) hydrosulfates, and subsequent changes in sulfate concentration fluctuated while the 207

Fe3+ continued to precipitate (Fig. 4c). A net increase in the concentration of soluble sulfate 208

was distinct only after 4 months (Fig. 4c). The initial increase in the pH was due to proton 209

consumption coupled with Fe2+ oxidation, whereas the decrease in the pH after 5 days was 210

attributed to Fe(III)-precipitation in the form of schwertmannite (eqn. [4]) or jarosite (eqn. 211

[5]) (Fig. 4b). The pH did not decrease to a prohibitively low pH value (≈ pH <1.2) in this 212

experiment. The long time course reflects the slow precipitation of Fe(III), which also 213

removes sulfate from the solution phase and thereby masks any net increase in sulfate 214

concentration until Fe(III) precipitation approaches equilibrium conditions. 215

216

3.3. Redox coupling between S0 and Fe3+ at 4°C 217

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Previous experiments in this study showed that the subambient incubation temperature 218

slowed down bacterial metabolism to the extent that it should be possible to discern major 219

phases in redox reactions due to substrate conversions. Thus, the possibility was explored that 220

Fe3+ was an external electron acceptor for S0 oxidation in growing cultures of strain SS3. 221

When the SS3 culture was grown at 4ºC with S0 and amended with Fe3+, the apparent 222

formation of soluble sulfate was delayed until the low concentration of Fe2+ (10 mM) carried 223

over with the inoculum was completely oxidized (Fig. 5a,c). The pH decreased in two phases 224

(Fig. 5a,b): (a) the initial pH decrease was attributed to ferric iron hydrolysis and 225

precipitation (eqns. 3 and 4) and (b) the latter phase was attributed to sulfuric acid formation 226

from S0 oxidation (eqns. 1 and 2). The first phase, Fe2+ oxidation and Fe3+ precipitation, 227

resulted in partial removal of soluble sulfate via precipitation as Fe(III) hydroxysulfates, 228

which masked fractional increases in sulfate formation upon initial S0 oxidation. As sulfur 229

oxidation ensued, the pH gradually decreased to low levels, which were increasingly 230

prohibitive to Fe2+ oxidation. The decrease in pH to <1.2 was found to be inhibitory to 231

Acidithiobacillus strain SS3 in this and other Fe2+ oxidation experiments such that some Fe2+ 232

accumulated in the medium toward the end of the incubation. This suggested that S0 233

oxidation was coupled with reduction of Fe3+ to Fe2+ due to parallel sulfur oxidation (Fig. 5c). 234

Thus, the low pH brought about by S0 oxidation slowed down Fe2+ re-oxidation (i.e. the 235

recycling of Fe2+ and Fe3+), while the S0-dependent Fe3+ reduction continued. In the 236

corresponding sterile control, the concentration of Fe2+ remained below the detection limit of 237

36 µM (2 mg Fe2+ L-1) (based on parameters of linear regression of the calibration line) [8]. 238

Parallel changes in Fe3+ concentration (Fig. 5d) showed an initial decrease followed by a 239

steep increase when S0 oxidation ensued. Fe(III)-hydroxysulfates that were precipitated in the 240

preceding stage of Fe2+ oxidation were re-dissolved when the pH decreased to <1.4 for 241

several months, causing the Fe3+ concentration to increase (Fig. 5d). The final concentration 242

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of Fe3+ was close to the sum of the initial concentrations of Fe2+ + Fe3+. In the chemical 243

control, ferric iron precipitated and did not re-dissolve because the pH remained at ~2.3 244

through the time course. 245

246

4. Discussion 247

248

This study addresses the oxidation of tetrathionate and S0 by Acidithiobacillus strain SS3 249

at low temperatures, an important subject matter to characterize because of bioleaching and 250

acid rock drainage in boreal mine sites. Temperature gradient experiments showed that 251

Acidithiobacillus strain SS3 could oxidize tetrathionate and S0 even at 5°C. The temperature 252

optima for tetrathionate and S0 oxidation were between 20º and 25ºC and were consistent 253

with the previous finding that Acidithiobacillus strain SS3 is psychrotolerant [24]. The broad 254

temperature optimum for S0 oxidation suggested that the oxidation rate was not solely 255

dependent on the temperature. It was possible that the oxidation rate may have also been 256

limited by the available surface area for the microorganisms to attach to the solid S0 particles 257

required for oxidation to occur. The upper permissive temperature for a number of pure and 258

mixed cultures of A. ferrooxidans has been demonstrated to range between 36.1 and 43.6ºC 259

[26]. The activation energies calculated for tetrathionate metabolism of 89 and 61 kJ mol-1 260

were lower than that calculated for abiotic tetrathionate oxidation of 105 kJ mol-1 at pH 1.5 261

[10]. The Ea values for tetrathionate and sulfur metabolism were both greater than the 38 kJ 262

mol-1 calculated for Fe2+ oxidation by washed cell suspensions of Acidithiobacillus strain SS3 263

[24]. Cultures growing with Fe2+ have typically yielded Ea values in the 80 kJ mol-1 range, 264

clearly suggesting a strong temperature dependency of iron oxidation by A. ferrooxidans [3]. 265

In previous studies of S0 oxidation, Ea values for several chemolithotrophic acidophiles 266

including A. ferrooxidans, Acidithiobacillus caldus, and Acidithiobacillus thiooxidans ranged 267

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from 26 to 72 kJ mol-1 [2, 15]. In addition to possible surface area limitation, the underlying 268

basis of temperature dependence of S0 may be a complex subject to interpret because solid 269

substrate oxidation additionally involves cell attachment, which may also respond to the 270

temperature. In the case of acidophilic iron and sulfur oxidizers, the thermodynamic 271

properties and temperature sensitivity of cellular attachment have yet to be elucidated. 272

Our experimental results indicated that substantial S0 oxidation was delayed until the 273

available Fe2+ had been oxidized. There are planktonic and sessile cells in the S0 culture, and 274

it is unclear whether all cells are equally capable of oxidizing Fe2+. A. ferrooxidansT rus 275

genes involved in Fe2+ oxidation are more highly expressed in Fe2+ media but are also present 276

in S0 grown cells [43], but similar information on the genes involved in S0 oxidation is not 277

available. Proteomic studies have shown that several proteins of A. ferrooxidans are 278

upregulated or downregulated depending on whether growth is dependent on Fe2+ or S0 [40]. 279

The differences in the Fe2+ oxidation rates of 67 mM Fe2+ in Fig. 4 (a rate in line with 280

previous data [24]) and 10 mM Fe2+ in Fig. 5 may have an explanation in differential 281

expression of genes responsible for Fe2+ and S0 oxidation. This may occur with available 282

substrate concentrations and the 10 mM Fe2+ situation may conceivably involve low level of 283

expression of the corresponding Fe2+ oxidation gene(s). Regardless of rate differences, both 284

experiments also indicated preferential oxidation of Fe2+ over S0, which may have 285

consequences for the bioleaching of sulfide minerals as the initial intermediates include 286

polysulfides and S0 as well as polythionates [23, 34]. While these differences in substrate 287

oxidation rates cannot be interpreted with certainty with the data available, they warrant 288

further research on multiple substrate conditions, an inevitable situation in bioleaching 289

processes. Solid-phase sulfur intermediates may passivate mineral surfaces [42] and thus 290

reduce the bioleaching rate because these sulfur species may not be efficiently removed until 291

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the available Fe2+ has been oxidized. The dynamics of iron and sulfur oxidation and reduction 292

in bioleaching situations is complex as it involves solid and solution phase reactions. 293

In this study, Acidithiobacillus strain SS3 utilized three different electron donor/acceptor 294

pairs at suboptimal temperatures, namely Fe2+/O2, S0/O2, and S0/Fe3+. The cultures were 295

grown under fully aerobic conditions as previous measurements of Fe2+ oxidation at higher 296

rates with a similar experimental setup demonstrated 95% O2 saturation [24]. The S0/Fe3+ 297

couple represents a mechanism of S0 oxidation whereby the electrons from S0 proceed via 298

carriers to Fe3+ reduction. The ability to reduce Fe3+ with S0 was already reported for A. 299

ferrooxidans by Brock and Gustafson [6]. As a result of the low pH and high Fe3+/Fe2+ ratio 300

after approximately 100 days, the medium redox potential measured by Pt-Ag/AgCl system 301

reached 650 mV (equivalent to 840 mV with the SHE), suggesting that the Fe3+/Fe2+ redox 302

pair could be thermodynamically competitive with the O2/H2O couple as an electron acceptor 303

during bacterial sulfur oxidation. 304

Different strains of A. ferrooxidans and ‘A. ferrivorans’ can have highly variable rates of 305

Fe2+ and S0 oxidation under aerobic and anaerobic conditions depending on their growth 306

history [38]. Sugio and co-workers [35-37, 39] reported the presence of a ferric ion reducing 307

system that catalyzes the reduction of Fe3+ with S0 in A. ferrooxidans. The authors proposed a 308

sulfur oxidation mechanism involving Fe3+ reduction via the sulfide:ferric ion 309

oxidoreductase, sulfur:ferric ion oxidoreductase, and sulfite:ferric ion oxidoreductase systems 310

in A. ferrooxidans. The accumulation of Fe2+ in media was observed under anaerobic 311

conditions and under aerobic conditions in the presence of inhibitors of the bacterial iron 312

oxidation enzyme system [35-37]. In the present study, the accumulation of Fe2+ from Fe3+ 313

reduction may have resulted from the decrease in pH to low values prohibitive to iron 314

oxidation [32] and relatively slow S0 oxidation and sulfate removal due to Fe(III)-315

precipitation. Sand [32] reported substantial accumulation of Fe2+ at pH <1.3 in aerobic A. 316

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ferrooxidans cultures which were supplemented with both S0 and Fe3+, again suggesting that 317

sulfur oxidation by A. ferrooxidans under oxic conditions is coupled with Fe3+ reduction. Fe2+ 318

oxidation may have been inhibited under these particular conditions because of the 319

prohibitively low pH value. 320

As shown in this work, subambient incubation temperatures allow temporal isolation of 321

redox reactions and pH changes associated with single and dual substrate oxidation, and 322

precipitation and chemical reactions are also relatively slow. Under these low temperature 323

and low pH conditions, it was possible to demonstrate the coupling between S0 oxidation and 324

Fe3+ reduction. The temperature dependence of the oxidation of solid-phase and soluble 325

substrates by Acidithiobacillus strain SS3 can be characterized by activation energy values 326

within a similar range, although the underlying biochemical oxidation mechanisms are very 327

different. The low temperature oxidation of the staple substrates of A. ferrooxidans and ‘A. 328

ferrivorans’, inorganic iron and sulfur compounds has relevance in management of 329

biogeochemical reactions in acid mine drainage in the arctic climate where the prevailing 330

temperatures are dominantly suboptimal for typical mesophilic microorganisms. How these 331

suboptimal temperatures impact the biological leaching reactions in bioleach mines remains 332

unclear. The oxidative acidic leaching reactions are highly exergonic and consequently heat 333

evolution in the interior zones of sulfide ore heaps as well as gob piles is inevitable even in 334

the winter time [20]. Strains such as the psychrotrophic Acidithiobacillus strain SS3 offer a 335

biological tool to simulate biogeochemical reactions and control iron and sulfur oxidation 336

rates at low temperatures, a mission that is impossible to accomplish with strictly chemical 337

reaction sequences. 338

339

Acknowledgements 340

341

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We thank S. Sääf for expert technical assistance. D. Kupka acknowledges research 342

support from the Science and Technology Assistance Agency (contract number APVV-51-343

027705) and the VEGA Agency projects No-2/0159/08. Work carried out at Umeå University 344

and the Tampere University of Technology was within the European Commission project 345

‘BioMinE’ under the Sixth Framework Program for Research and Development (European 346

project contract NMP1-CT-500329-1). O.H. Tuovinen was supported in part by the Finnish 347

Funding Agency for Technology and Innovation (Finland Distinguished Professor Program, 348

402/06). 349

350

References 351

352

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475

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FIGURE LEGENDS 476 477 Fig. 1 Temperature gradient results for (a) tetrathionate oxidation rates by Acidithiobacillus 478

strain SS3 at 5° and 30°C; Ratkowsky plots (time in hours) of the relationship between 479

temperature and tetrathionate calculated for (b) tetrathionate metabolism and (c) pH decrease; 480

and (d) Ratkowsky plots for S0 oxidation as measured by the decrease in pH. The solid lines 481

in panels (b), (c) and (d) represent the best fit of the linear portion of the tetrathionate and S0 482

oxidation rates. 483

484

Fig. 2 Arrhenius plots for the metabolism of tetrathionate and sulfur. Tetrathionate 485

metabolism was measured by a decrease in the tetrathionate concentration by cyanolysis (a) 486

and a decrease in pH (b), whereas S0 oxidation was calculated using an increase in sulfate 487

concentration (c) and a decrease in pH (d). 488

489

Fig. 3 Time course of (a) 5 g S0 L-1 (156 mM) oxidation by Acidithiobacillus strain SS3 at 490

4ºC inoculated from a ferrous-iron-grown culture at 4°C plotted as the log sulfate 491

concentration ( ) and the Fe2+ concentration ( ); (b) corresponding changes in pH (b). 492

Open symbols indicate abiotic control. Data points are averages ± SD (n = 3). 493

494

Fig. 4 Fe2+ oxidation by Acidithiobacillus strain SS3 in the presence of S0 at 4°C inoculated 495

from a ferrous-iron-grown culture at 4°C. Initially, the medium contained 156 mM S0 and 67 496

mM Fe2+. Symbols are: a: Fe2+ ( ), Fe3+ ( ), and total iron ( ); b: pH ( ) and redox ( ); 497

and c: sulfate plotted as the semilog ( ). Data points are averages ± SD (n = 3). 498

499

Fig. 5 Time course of S0 oxidation coupled with Fe3+ reduction by Acidithiobacillus strain 500

SS3 at 4ºC inoculated from a ferrous-iron-grown culture at 4°C: (a) sulfate; (b) pH; (c) Fe2+; 501

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(d) Fe3+. Open symbols indicate sterile controls. Data points are averages ± SE (n = 2). 502

Initially, the medium contained 156 mM S0 and 35 mM Fe3+. About 10 mM Fe2+ was carried 503

over with the inoculum to the culture medium. No Fe2+ was added to the uninoculated control 504

and the Fe2+ concentration in the control was below the detection limit for the entire 505

experiment. 506

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