1 inhibition of aspergillus niger phosphate solubilization by fluoride
TRANSCRIPT
1
Inhibition of Aspergillus niger phosphate solubilization by fluoride released from rock 1
phosphate 2
Running title: Inhibition of fungal P solubilization by fluoride 3
4
Gilberto de Oliveira Mendesa, Nikolay Bojkov Vassilevb, Victor Hugo Araújo Bondukia, 5
Ivo Ribeiro da Silvac,e, José Ivo Ribeiro Júniord, Maurício Dutra Costaa,e# 6
7
a Department of Microbiology, Federal University of Viçosa, Brazil 8
b Department of Chemical Engineering, Faculty of Sciences, University of Granada, Spain 9
c Department of Soil Science, Federal University of Viçosa, Brazil 10
d Department of Statistics, Federal University of Viçosa, Brazil 11
e Researcher of the National Council for Scientific and Technological Development 12
(CNPq), Brazil 13
14
Abstract 15
The simultaneous release of various chemical elements with inhibitory potential for 16
phosphate solubilization from rock phosphate (RP) was studied in this work. Al, B, Ba, Ca, 17
F, Fe, Mn, Mo, Na, Ni, Pb, Rb, Si, Sr, V, Zn, and Zr were released concomitantly with P 18
during the solubilization of Araxá RP (Brazil), but only F showed inhibitory effects on the 19
process at the concentrations detected in the growth medium. Besides P solubilization, 20
# Corresponding author: Laboratório de Associações Micorrízicas, Instituto de Biotecnologia
Aplicada à Agropecuária (BIOAGRO), Av. P. H. Rolfs, s/n, Campus, Viçosa, MG, 36570-000, Brazil. E-mail: [email protected]. Telephone: +55 31 38992965
Copyright © 2013, American Society for Microbiology. All Rights Reserved.Appl. Environ. Microbiol. doi:10.1128/AEM.01487-13 AEM Accepts, published online ahead of print on 14 June 2013
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fluoride decreased fungal growth, citric acid production, and medium acidification by A. 21
niger. At the maximum concentration found during Araxá RP solubilization (22.9 mg F- per 22
L), fluoride decreased P solubilization by 55%. These findings show that fluoride 23
negatively affects RP solubilization by A. niger through its inhibitory action on the fungal 24
metabolism. Given that fluoride is a common component of RPs, the data presented herein 25
suggest that most of the microbial RP solubilization systems studied so far were probably 26
operated under suboptimal conditions. 27
28
Keywords: fluorapatite, phosphate solubilization, fluoride, fungal metabolism, 29
fermentation process 30
31
Introduction 32
The use of phosphate-solubilizing microorganisms (PSM) is emerging as a 33
biotechnological alternative for producing soluble P-fertilizers from rock phosphate (RP) 34
(1). The ability of PSM to mobilize P from sparingly soluble sources can be a useful tool in 35
P-fertilization management. Some studies have shown that the product obtained from the 36
treatment of RP with PSM (2) or even the direct application of PSM to soil (3) can improve 37
plant growth and P uptake. This alternative is becoming increasingly important against a 38
backdrop of depletion of high-grade RP reserves. Despite the uncertainties of forecasts 39
about the depletion of these reserves, ranging between 30 and 300 years, there is a 40
consensus that the accessibility and quality of RPs are decreasing and, consequently, 41
production costs of P-fertilizers are rising (4). Therefore, efficient processes, including 42
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microbially-mediated ones, able to exploit lower-grade RPs and/or alternative P-sources (5) 43
at low cost should be developed in the near future. 44
Rock phosphates differ in chemical and mineralogical characteristics depending on 45
the location where they are collected. The basic unit is apatite [Ca10(PO4)6(Z)2], which is 46
classified as fluoroapatite, chloroapatite, or hydroxyapatite when Z is F, Cl, or OH (6). In 47
addition to apatite, the RPs contain significant amounts of numerous other chemical 48
elements (7). In some RPs, the concentration of these accompanying elements can be quite 49
high and include some toxic elements, e.g. uranium, cadmium, and a number of other heavy 50
metals (4, 7). Reyes et al. (8) suggested that the presence of toxic elements in RP could 51
inhibit fungal growth and, consequently, P solubilization. However, to exert any effect, 52
these elements first have to be mobilized, but so far, no reports of which elements are 53
actually released during microbial RP solubilization have been published. Some of these 54
accompanying elements are presumably released together with P during RP solubilization 55
and could inhibit the process. This fact could explain the lower solubilization rate of RPs 56
when compared to that of pure synthetic apatites (9). 57
The main mechanisms of microbial P solubilization include the production of 58
organic acids, which have the ability to form stable complexes with cations that form 59
poorly soluble compounds with P (10, 11), and, to a lesser extent, the release of protons 60
(H+) into the medium (12). Some elements that may be released during RP solubilization 61
could affect these mechanisms by promoting changes in microbial metabolism (13). 62
Schneider et al. (9) observed lower production of citric and gluconic acids by A. niger when 63
comparing the solubilization of RPs to that of pure synthetic apatite. Elements like Cu, Fe, 64
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Mn, and Zn, even at low concentrations, inhibit the production of organic acids by fungi 65
(14, 15) and could be involved in the lower production observed by Schneider et al. (9). 66
Furthermore, Illmer and Schinner (12) proposed that P solubilization by some microbial 67
species is based on the release of H+ resulting from processes related to biomass 68
production, such as respiration or NH4+ assimilation. Thus, the inhibition of microbial 69
growth could result in a decreased release of H+ into the medium and, consequently, 70
diminished P solubilization. 71
Past studies with PSM have overlooked the potential inhibitory effect of elements 72
released during microbial RP solubilization. A better understanding of the P solubilization 73
process can lead to new perspectives on strategies to improve its efficiency. Thus, the 74
objective of this work was to determine which chemical elements are released during 75
fungal RP solubilization and to evaluate the effects of these elements on the P solubilization 76
by A. niger. 77
78
Materials and Methods 79
Microorganism and cultivation conditions 80
The isolate Aspergillus niger FS1 was obtained from the Collection of Phosphate 81
Solubilizing Fungi, Institute of Biotechnology Applied to Agriculture (BIOAGRO), Federal 82
University of Viçosa, Viçosa, MG, Brazil. Batch fermentations were conducted in 125-mL 83
flasks containing 50 mL of the National Botanical Research Institute's phosphate growth 84
medium (NBRIP) (16) (10 g glucose, 5 g MgCl2.6H2O, 0.25 g MgSO4.7H2O, 0.2 g KCl, 0.1 85
g (NH4)2SO4, 1 L deionized water). The P source in the NBRIP growth medium used in the 86
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present experiments was either Araxá RP or K2HPO4. The medium pH was adjusted to 7.0 87
before the application of the P source. The flasks were inoculated with 106 conidia from a 88
conidial suspension prepared in 0.1% (v/v) Tween 80. All flask cultures were incubated on 89
an orbital shaker at 160 rpm at 32 °C. 90
91
Rock phosphate characterization 92
RP from Araxá (Brazil) was used in the solubilization studies. Chemical analyses 93
(see listing in Table 1) were done after the digestion of an RP sample with aqua regia acid 94
solution (3 HCl : 1 HNO3) or lithium metaborate (17). The concentration of the chemical 95
elements was determined by inductively coupled plasma optical emission spectrometry 96
(ICP-OES) and inductively coupled plasma mass spectrometry (ICP-MS), except for P, 97
which was determined by an ascorbic acid method (18), and for Cl- and F-, which were 98
determined with specific ion electrodes. 99
The mineralogical composition was determined by powder X-ray diffraction (XRD) 100
in a multifunctional Panalytical X’Pert Pro PW 3040/60 diffractometer equipped with a 101
1800 W, 60 kV cobalt tube (Co-Kα radiation, λ = 1.790269 Å) operated at 40 kV and 30 102
mA. Powder samples were mounted in holders in order to minimize preferred orientation, 103
and the scans were performed in a step-by-step mode from 4o to 80o 2θ with 104
0.05o increments per 2 s. 105
106
Kinetics of rock phosphate solubilization 107
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Some elements were prioritized based on their biological significance in order to 108
simplify further analyses. Among the 63 elements detected in Araxá RP, 10 were excluded 109
for being below the detection limit when 3 g L-1 of RP were added to the medium (Ag, Au, 110
Bi, Cs, In, Sb, Sn, Te, Tl, and W). Of the 53 remaining elements, besides P, 28 were 111
selected for analysis: Al, As, B, Ba, Be, Ca, Cd, Co, Cr, Cu, F, Fe, Ga, K, Li, Mg, Mn, Mo, 112
Na, Ni, Pb, Rb, S, Si, Sr, V, Zn, and Zr. 113
The kinetics study was conducted for 10 days in NBRIP medium supplemented with 114
3 g L-1 of RP. In all, 66 flask cultures were set up and, every 12 hours, three flasks were 115
removed from the shaker for analyses. The spent medium was passed through 0.45-µm 116
membranes by vacuum filtration and analyzed for pH and the chemical elements released. 117
The fungal biomass retained on the membranes was collected, dried in an oven at 70 °C to 118
constant weight, and incinerated at 500 °C for 6 h. Biomass yield was determined by 119
subtracting from the weight of dried fungal mycelium the weight of the residue left after its 120
incineration. This method avoids overestimation due to the adherence of phosphate 121
particles to the mycelium (19). Uninoculated flasks from the beginning and end of the 122
experiment were used as controls in the determination of the solubilized elements. 123
124
Screening of chemical elements affecting rock phosphate solubilization 125
The chemical elements released during the kinetics study were combined in a 126
factorial experiment in order to screen which ones affect the RP solubilization. Due to the 127
large number of elements, a Plackett-Burman design (PBD) was chosen for forming the 128
combinations of elements in the treatments. The PBD is a fractional factorial design where 129
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n factors are combined at two levels in at least n+1 treatments for estimating the main effect 130
(linear coefficient) of each factor, excluding the interactions between them (20). Thus, each 131
one of the 17 elements was added at two coded levels: -1, absence of the element, and 1, 132
maximal concentration of the element achieved over the entire kinetics study (Table 2). The 133
combinations of elements in the treatments (Table S1) were created using the option DOE 134
(design of experiments) of the statistical software Minitab 16. A central point (mean 135
between levels -1 and 1, coded as 0) was added to the experiment and replicated five times 136
in order to determine the experimental error, but was not included in the adjusted model. 137
The main effects of the elements on P solubilization were estimated through regression 138
analysis by the method of least squares. The option DOE of the software Minitab was used 139
to analyze the data and the results were interpreted based on the significance (p < 0.05) of 140
the regression coefficient of each element in the fitted equation. The model adopted was: 141
where, yijm is the value of solubilized P observed in the run i with the combination of n 142
chemical elements at level xm, β0 is the regression constant, βj is the regression coefficient 143
of the linear effect of each factor (n chemical elements), m is the coded level of each 144
element (-1 or 1), and εijm is the experimental error associated with the observation yijm. 145
The experiment was conducted for 60 h in NBRIP medium supplemented with 3 g 146
L-1 of RP. For each element studied, a solution was prepared with the appropriate 147
concentration for adding 1 mL to flasks at level 1. The following chemicals were used: 148
AlCl3, H3BO3, BaCl2.2H2O, CaCl2.2H2O, KF.2H2O, FeCl3, MnCl2.4H2O, 149
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(NH4)6Mo7O24.4H2O, NaCl, NiCl2, Pb(NO3)2, RbCl, K2SiO3, SrCl2.6H2O, V standard 150
solution (Spectrum®), ZnCl2, and Zr standard solution (Vetec®). The solutions were 151
prepared in ultrapure water and all glassware was washed in 2% HCl before use. Given the 152
low concentration of most elements, changes in the medium composition by the 153
accompanying ions were negligible. The flasks were filled with 25 mL of a double-154
concentrated NBRIP medium and, after the addition of the corresponding element 155
solutions, were made up to 50 mL with ultrapure water. At the end of the experiment, the 156
spent medium was filtered through quantitative filter paper (phosphorus-free, 15-17 µm 157
pores), and the solubilized P in the filtrate was determined as described above. 158
159
Effect of fluoride on RP solubilization and metabolism of A. niger 160
The effect of fluoride on the solubilization process was studied under two 161
cultivation conditions by varying the P source. The experiment was conducted for 60 h in 162
NBRIP medium supplemented with 3 g RP per L or 1 g K2HPO4 per L. NaF was added to 163
the medium at concentrations ranging from 0 to 50 mg of fluoride per liter, with increments 164
of 5 mg L-1. At the end of the experiment, solubilized P and the pH were determined in the 165
treatments with RP. The P/Biomass yield (YP/X) was calculated from the ratio of solubilized 166
P (mg) to fungal biomass produced (g). The fungal biomass and the production of organic 167
acids were determined in the treatments that received K2HPO4 as a P source. The 168
experiment was conducted using an entirely randomized design with three replicates at the 169
central point (25 mg F per L), followed by regression analysis. 170
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Organic acids were determined by UPLC/MS/MS using a UPLC Acquity system 171
coupled to a Xevo TQS mass spectrometer (Waters, Milford, MA, USA). Based on the 172
previous characterization of the isolate A. niger FS1 (21), the analysis was focused on 173
citric, gluconic, and oxalic acids. Chromatographic separations were performed using an 174
Acquity UPLC BEH C18 column (1.7 μm, 2.1 mm x 100 mm) under the following 175
conditions: mobile phase 0.1% phosphoric acid, flow 0.2 mL min-1, sample injection 176
volume 10 µL, and analysis time 3.5 min. Mass spectrometry was performed under the 177
following conditions: source electrospray (ESI), source temperature 150 ºC, desolvation 178
temperature 300 ºC, cone gas flow 150 L h-1, desolvation gas flow 500 L h-1, collision gas 179
flow 0.14 mL min-1, mode positive. 180
181
Results 182
Rock phosphate characterization 183
The chemical analyses revealed a complex constitution of the Araxá RP (Table 1). 184
Among 66 elements investigated, only Cl, Hg, and Re were not detected. The RP contained 185
13.97% of P, with a molar Ca:P ratio of 1.67. This value is consistent with the theoretical 186
molar ratio of apatite [Ca5(PO4)3], showing that P is predominantly linked to Ca. However, 187
only 4% of the total P was soluble in 2% citric acid. The chemical analyses also showed 188
considerable concentrations of rare-earth elements (Ce, Dy, Er, Eu, Gd, Ho, La, Lu, Nd, Pr, 189
Sc, Sm, Tb, Tm, Y, and Yb) that probably became part of the apatite structure during rock 190
crystallization (7). Based on XRD and chemical analysis, the RP was classified as a 191
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fluorapatite with some mixture of hydroxyapatite, with the theoretical formula 192
Ca5(PO4)3(F,OH). 193
194
Kinetics of rock phosphate solubilization 195
High growth rates and a quick drop in the pH of the medium from 5.5 to 3.2 196
occurred in the first 36 h of incubation (Fig. 1). The concentration of solubilized P 197
increased rapidly in the first 60 h, reaching approximately 80 mg L-1. Afterwards, the pH 198
dropped slightly, and the P concentration increased and decreased to different extents at 199
irregular intervals. The biomass continued to grow at a slower rate after the first 60 h. 200
Fungal biomass increased during four successive intervals over the course of the 201
experiment: 0-36, 48-120, 132-180, and 192-240 h (Fig. 1). The first hours of the second 202
(48-120 h) and the third (132-180 h) growth intervals coincided with the decreases in 203
solubilized P in the medium. 204
During RP solubilization, 17 chemical elements were released (Table 2) and most 205
presented a pattern similar to that of P (Figs. 1, 2). The correlations between the 206
concentrations of these elements and that of P were higher than 0.7 (p < 0.01) (Table S2). 207
Low concentrations of B, Mo, Ni, Pb, Rb, V, Zn, and Zr were detected in the medium 208
during incubation (Table S3), reflecting their low concentrations in the Araxá RP (Table 1). 209
In fact, at an initial RP dose of 3 g L-1, these elements, except for B and Zr, were expected 210
to be released into the medium at concentrations lower than 1 mg L-1. As, Be, Cd, Co, Cr, 211
Cu, Ga, and Li were not released in detectable quantities. The concentrations of K, Mg, and 212
S in the medium after RP dissolution were also determined, but the data are not presented 213
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here because these elements are also constituents of the NBRIP medium and showed 214
practically no variation during incubation. 215
216
Screening of chemical elements affecting rock phosphate solubilization 217
Due to the higher solubilization rate observed during the first 60 h of incubation and 218
the fluctuations in solubilized P observed thereafter (Fig. 1), the study of the effects of the 219
released elements on RP solubilization was limited to that time interval. For this, a stressful 220
condition was established by adding each element to the medium at the highest 221
concentration recorded during RP solubilization (Table 2). Given that the concentration of 222
each element rose from 0 to a maximum value concomitantly with the increases in P 223
concentration, the amount of each element initially added to the medium for the screening 224
was higher than the actual concentration that would be found at a particular time and 225
without supplementation. This overestimation, however, was intentionally introduced to 226
facilitate the identification of potentially inhibitory elements that might exert their effects at 227
some point during the solubilization of Araxá RP. If a given element was not inhibitory at 228
the maximum concentration used in the screening, it would not be inhibitory at lower 229
concentrations. 230
Among the 17 elements screened, only F and Sr exerted significant effects on the 231
level of solubilized P (Fig. 3). A positive regression coefficient was observed for Sr, 232
indicating that it stimulates RP solubilization. On the other hand, the regression coefficient 233
for F was negative and presented a high value, resulting in a decrease of 81% in the mean 234
of solubilized P in the treatments where fluoride was added at level 1 (Fig. 3). This strong 235
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inhibitory effect of F is evident when comparing the values of solubilized P in the 236
treatments with and without this element (Table S1). 237
238
Effect of fluoride on RP solubilization and metabolism of A. niger 239
Given the observations on the inhibitory effect of fluoride, another set of 240
experiments was performed to evaluate the effects of different fluoride doses on RP 241
solubilization. Besides Araxá RP, a soluble P source, K2HPO4, was used to evaluate the 242
effects of fluoride on the metabolic processes involved in RP solubilization in a less 243
complex medium. The results clearly reflected decreases in medium acidification and RP 244
solubilization when fluoride doses were increased (Fig. 4a). Additionally, NaF and KF 245
were compared in order to rule out a possible effect of the counter ion in the fluoride 246
source, but no difference in RP solubilization was detected between the two salts (data not 247
shown). At the dose corresponding to the maximal fluoride concentration detected during 248
the solubilization process (22.9 mg fluoride per liter, Table 2), a decrease of about 55% in 249
solubilized P was estimated from the adjusted regression equation (Fig. 4a). At this fluoride 250
concentration, a decrease of about 75% in fungal growth was found (Fig. 4b). Furthermore, 251
increasing fluoride concentrations resulted in lower yield of solubilized P per unit of 252
biomass (YP/X) (Fig. 4b). 253
The data show that the production of citric acid was almost completely inhibited at 254
fluoride concentrations higher than 20 mg L-1 while the production of gluconic and oxalic 255
acids was stimulated by concentrations of up to 35 mg L-1 (Fig. 4c). 256
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Discussion 258
The release of chemical elements concurrent with P during microbial RP 259
solubilization has received little attention in past studies. In this work, it has been clearly 260
demonstrated that various chemical elements are released together with P. Among them, F 261
significantly lowered the levels of solubilized P. Fluoride is toxic to microbial cells, 262
affecting a series of physiological processes (22). Fluoride toxicity to bacteria and fungi 263
results most likely from blocking the functions of enzymes (23), such as enolase (24), 264
peroxidase (25), heme oxidases (22), ATPases (26), phosphatases (22), and copper-265
enzymes such as polyphenol oxidases (27). The inhibition results from direct HF/F- binding 266
or by metal-F complex binding (22). 267
Under the conditions reported herein, fluoride affects metabolic processes directly 268
involved in RP solubilization. As reported for other fungal species (23, 28), the increase in 269
fluoride concentrations resulted in less growth of A. niger. Furthermore, at high fluoride 270
doses, the biomass became less effective at RP solubilization, given that the amount of P 271
solubilized per unit of biomass was less (Fig. 4b). These observations are presumably 272
related to the lower medium acidification and lower production of citric acid detected at 273
higher fluoride doses. As these changes affected the solubilization agents, namely H+ and 274
citric acid levels, it is reasonable to conclude that the concurrent mobilization of fluoride 275
during the solubilization of Araxá RP decreased the efficiency of the process. 276
Different responses were observed for the production of organic acids by the isolate 277
A. niger FS1 when exposed to fluoride. The production of citric acid, one of the most 278
effective agents for the release of P from RP (29), was almost completely inhibited at the 279
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highest fluoride concentration (22.9 mg L-1) detected during the experiment on RP 280
solubilization kinetics (Fig. 4c). Agrawal et al. (30) reported similar results and suggested 281
that the decrease in citric acid production by NaF resulted from the inhibition of enolase 282
activity, which is involved in the conversion of 2-phosphoglycerate (2-PG) to 283
phosphoenolpyruvate (PEP), thus disrupting the supply of precursors for citric acid 284
production. Interestingly, the production of gluconic and oxalic acids was stimulated by 285
increasing fluoride concentration up to 35 mg L-1 (Fig. 4c). The synthesis of gluconic acid 286
is catalyzed by the extracellular enzyme glucose oxidase (GOD), which converts glucose 287
into gluconic acid (31). Thus, the positive effect of fluoride on the production of gluconic 288
acid may result from the surplus of glucose in the medium due to the inhibition of fungal 289
growth. However, the reason for the stimulatory effect of fluoride on oxalic acid production 290
remains unclear. The synthesis of this organic acid is catalyzed by the enzyme 291
oxaloacetase, which converts oxaloacetate into oxalate and acetate. The reaction takes place 292
in the cytoplasm and does not involve the tricarboxylic acid (TCA) cycle, since A. niger is 293
capable of forming oxaloacetate from pyruvate and CO2 through a cytoplasmic, constitutive 294
pyruvate carboxylase (32). Given the putative partial inhibition of glycolysis and, 295
consequently, of the TCA cycle, the supply of oxaloacetate precursors must come from 296
alternative sources, a hypothetical one being the gluconic acid produced. Aspergillus niger 297
possesses a modified (non-phosphorylating) Entner-Doudoroff pathway in which gluconate 298
is converted to glyceraldehyde and pyruvate in two steps (33). Pyruvate could be 299
subsequently converted into oxaloacetate by pyruvate carboxylase and, then, oxaloacetate 300
cleaved into oxalate and acetate by oxaloacetase. Müller (34) demonstrated that A. niger 301
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can use gluconic acid as a C source and accumulate oxalate as an end-product. However, 302
this author failed to detect the enzymes of the Entner-Doudoroff pathway and of the non-303
phosphorylating Entner-Doudoroff system in cell-free extracts of his A. niger strain (35). 304
Differently from Elzainy et al. (33), Müller (35) added gluconic acid to the medium after 305
fungal growth on glucose, which explains the absence of the enzymes that were shown to 306
be inducible by gluconate (33). The conversion of glucose into gluconic acid and its 307
subsequent use through the non-phosphorylating Entner-Doudoroff system could be an 308
alternative for A. niger to overcome the inhibition of glycolysis caused by fluoride. Further 309
studies are necessary to confirm this hypothesis. 310
Differently from fluoride, Sr had a positive effect on RP solubilization. This element 311
has no apparent biological function, being non-specifically accumulated in the biomass of 312
filamentous fungi and yeasts (36). It can act as a Ca analogue in some situations (37) and 313
can mitigate the inhibitory effects of Na on fungal growth (38). However, the Na 314
concentration found in the medium (Table 3) was not high enough to inhibit fungal growth 315
(38). The effect of Sr was probably more closely related to the chemical equilibrium in the 316
medium. Since Sr stimulated RP solubilization, albeit at a low level, an exhaustive 317
exploration of this issue was not a concern in the present work. 318
The dynamic variations of the medium conditions due to changes in the A. niger 319
metabolism and in the chemical equilibria are probably the reasons for the variations in the 320
solubilized P concentrations observed throughout the entire incubation (Fig. 1). Vassilev et 321
al. (39) observed that decreases in soluble P in the fermentation medium were accompanied 322
by decreases in titratable acidity and suggested that this resulted from the consumption of 323
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organic acid by the fungus under C depletion. The data obtained in our work support this 324
hypothesis since the decreases in soluble P apparently occurred in response to the 325
beginning of a new growth cycle, when the fungus may have used part of the organic acids 326
in its metabolism. Organic acids affect P solubility by forming complexes with metal 327
cations in solution, thereby avoiding the precipitation of metal phosphates (11). 328
Furthermore, Illmer and Schinner (12) showed that changes in the medium conditions 329
during the solubilization of P-Ca minerals (brushite and apatite) can lead to P 330
reprecipitation. The consumption of organic acids probably triggers the reprecipitation of 331
metal phosphates and, as a consequence, leads to a decrease in soluble P. The absence of 332
variation in the pH concomitantly to these reactions reinforces the hypothesis that the 333
changes in solubilized P depend mainly on the complexation of metal cations by organic 334
acids. 335
The fluctuations in the concentrations of some of the elements released from Araxá 336
RP followed a pattern similar to that of P (Figs. 1, 2). Al, Ba, Ca, Fe, and Sr can form 337
complexes of low solubility with P (40) and could be involved in P precipitation during the 338
periods of organic acid consumption discussed above. In the case of F, the reasons for the 339
decreases in its concentrations are not clear. As F is found predominantly as fluoride anions 340
(F-) in solution, one possible explanation is that it could form complexes of low solubility 341
with Ca2+ (CaF2) or Al3+ (AlF3) (41), which presumably would be released when organic 342
acids are consumed. Thus, during the dissolution of Araxá RP, cycles of solubilization and 343
precipitation of some ion pairs probably occur in accordance with their solubility. However, 344
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the extensive exploration of chemical equilibria in the medium was beyond the scope of 345
this work. 346
This is the first report showing the inhibitory effect of fluoride on RP solubilization. 347
It contributes to an understanding of the pronounced decrease in fungal solubilization of 348
RPs compared to that of pure synthetic apatite (9). The release of fluoride during microbial 349
RP solubilization has been ignored so far, even though most RPs contain high amounts of 350
fluoride. In fact, RP constitutes the main natural reserves of F (41). These findings open 351
new avenues for improving RP-solubilization efficiency through strategies for removing 352
fluoride during microbial solubilization or by selecting more fluoride-tolerant strains. 353
354
Conclusions 355
Among the various chemical elements mobilized during the solubilization of Araxá 356
RP by A. niger, only fluoride significantly lowered solubilization efficiency. Fluoride 357
decreased fungal growth, citric acid production, medium acidification, and P solubilization. 358
The data from this study show that fluoride limits the solubilization of Araxá RP by A. 359
niger by negatively affecting metabolic processes involved in phosphate solubilization. 360
Given the ubiquitous distribution of fluoride in RPs, most microbial RP-solubilization 361
systems studied so far have probably been operated at suboptimal conditions. 362
363
Acknowledgments 364
The authors are grateful to Dr. Maurício P. F. Fontes for his assistance in XRD analysis. 365
The authors are also thankful to the National Council for Scientific and Technological 366
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Development (CNPq) for financing this work and providing scholarships to the first and 367
last authors. Financial support for this study was also provided by Fundação de Amparo à 368
Pesquisa do Estado de Minas Gerais (FAPEMIG), project CAG-APQ-00712-12, and the 369
Spanish projects CTM2011-027797 and P09RNM-5196. 370
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Figure captions 479
Fig. 1. Solubilized phosphorus, changes in pH, and biomass accumulation during Araxá 480
rock phosphate solubilization by Aspergillus niger. Values are means of three replicates. 481
Error bars denote the standard deviation. 482
483
Fig. 2. Release of chemical elements during the solubilization of Araxá rock phosphate by 484
Aspergillus niger. 485
486
Fig. 3. Effects of chemical elements on the solubilization of Araxá rock phosphate by 487
Aspergillus niger. Data represent the means of solubilized P for each element at the levels -488
1 (absence of the element) and 1 (maximum concentration of the element achieved during 489
RP solubilization, Table 2). The linear regression coefficient of the element is presented at 490
the top of each graph (R² of regression: 0.88). * Significant by the t test (p < 0.05). 491
492
Fig. 4. Effect of fluoride on the solubilization of Araxá rock phosphate and the metabolism 493
of Aspergillus niger. (a) Solubilized P and medium pH after 60 h of cultivation in NBRIP 494
medium supplemented with 3 g L-1 RP. (b) Fungal biomass and P/Biomass yield (YP/X = 495
mg solubilized P per g of biomass). (c) Organic acids produced after 60 h of cultivation in 496
NBRIP medium supplemented with K2HPO4. All regression coefficients are significant by t 497
test (p < 0.01). 498
499
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Table 1. Chemical composition of Araxá rock phosphate.
Element mg kg-1 Element mg kg-1 Element mg kg-1
Ag 0.66
Gd 193.9
S 1050
Al 3032
Ge 3.7
Sb 0.12
As 13.5
Hf 30.5
Sc 38.3
Au 0.10
Hg 0.0
Se 6.5
B 374.5
Ho 17.2
Si 12080
Ba 20704
In 0.07
Sm 281.1
Be 12.7
K 600
Sn 10.8
Bi 0.06
La 1580
Sr 7622
Ca 302450
Li 1.5
Ta 27.1
Cd 0.89
Lu 2.0
Tb 22.5
Ce 3468
Mg 2700
Te 0.15
Cl < 20
Mn 1750
Th 240.4
Co 17.5
Mo 6.0
Ti 21600
Cr 136.8
Na 2967
Tl 0.60
Cs 0.35
Nb 1290
Tm 3.5
Cu 31.0
Nd 1689
U 70.4
Dy 113
Ni 55.5
V 131.5
Er 36.4
P 139700
W 7.1
Eu 70.0
Pb 27.4
Y 315.5
F 15931
Pr 435.3
Yb 17.0
Fe 59700
Rb 4.5
Zn 190.5
Ga 17.3
Re < 0.1
Zr 1564
Table 2. Maximum concentration of elements achieved during solubilization of Araxá rock
phosphate by Aspergillus niger. The study was done in 50 mL of NBRIP medium
supplemented with 3 g of rock phosphate (particle size < 75 µm) per liter. The flasks were
inoculated with 106 conidia from a conidial suspension prepared in 0.1% (v/v) Tween 80
and incubated on an orbital shaker at 160 rpm at 32 °C.
Element Al B Ba Ca F Fe Mn Mo Na Ni Pb Rb Si Sr V Zn Zr
Concentration
(mg L-1) 2.8 0.8 1.87 122.3 22.9 6.47 2.03 0.03 9.25 0.09 0.07 0.05 6.69 17.33 0.09 0.13 0.4
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