Sulfite oxidation catalyzed by aa(3)-type cytochrome c oxidase in Acidithiobacillus ferrooxidans

Sulfite is produced as a toxic intermediate during Acidithiobacillus ferrooxidans sulfur oxidation. A. ferrooxidans D3-2, which posseses the highest copper bioleaching activity, is more resistant to sulfite than other A. ferrooxidans strains, including ATCC 23270. When sulfite oxidase was purified homogeneously from strain D3-2, the oxidized and reduced forms of the purified sulfite oxidase absorption spectra corresponded to those of A. ferrooxidans aa(3)-type cytochrome c oxidase. The confirmed molecular weights of the α-subunit (52.5 kDa), the β-subunit (25 kDa), and the γ-subunit (20 kDa) of the purified sulfite oxidase and the N-terminal amino acid sequences of the γ-subunit of sulfite oxidase (AAKKG) corresponded to those of A. ferrooxidans ATCC 23270 cytochrome c oxidase. The sulfite oxidase activities of the iron- and sulfur-grown A. ferrooxidans D3-2 were much higher than those cytochrome c oxidases purified from A. ferrooxidans strains ATCC 23270, MON-1 and AP19-3. The activities of sulfite oxidase purified from iron- and sulfur-grown strain D3-2 were completely inhibited by an antibody raised against a purified A. ferrooxidans MON-1 aa(3)-type cytochrome c oxidase. This is the first report to indicate that aa(3)-type cytochrome c oxidase catalyzed sulfite oxidation in A. ferrooxidans.     

Ferrous iron oxidation and uranium extraction by Thiobacillus ferrooxidans

The microbiological oxidation of ferrous iron in batch and continuous systems has been investigated in relation to uranium extraction from a low-grade ore by Thiobacillus ferrooxidans. The influence of the parameters, agitation, and aeration on oxygen saturation concentration, rate of oxygen mass transfer, and rate of ferrous iron oxidation was demonstrated. The kinetic values, V_max and K were determined using an adapted Monod equation for different dilution rates and initial concentrations of ferrous iron. The power requirements for initial leaching conditions were also calculated. Uranium extraction as high as 68% has been realized during nine days of treatment. Regrinding the leach residue and its subsequent leaching yielded 87% uranium solubilization.     

Sulfur-dependent inhibition of protein and RNA synthesis by iron-grown Thiobacillus ferrooxidans

The addition of sulfur to iron-grown Thiobacillus ferrooxidans resulted in a rapid inhibition in the rates of protein synthesis and RNA synthesis. The inhibition of both functions was measured within 15 to 30 min and was maximal between 70 and 90% compared to the iron-grown controls. DNA synthesis, carbon dioxide fixation, and short-term ferrous oxidation rates of the bacteria growing on ferrous ions were not effected by sulfur addition, indicating that the sulfur addition was not perturbing general cellular energy metabolism. The inhibition caused by sulfur mimicked the effect of the RNA synthesis inhibitor, rifampicin, which inhibited both RNA and protein synthesis, but did not correspond with the translational inhibitor, chloramphenicol, which inhibited only protein synthesis in the first hour. Since chloramphenicol pretreatment did not block the sulfur effect, the inhibition of RNA synthesis following sulfur addition was not mediated through protein synthesis.     

Cytochrome oxidase of an acidophilic iron-oxidizing bacterium, Thiobacillus ferrooxidans, functions at pH 3.5

Cytochrome oxidase of Thiobacillus ferrooxidans was partially purified. The oxidase preparation had haems a and c, and oxidized ferrocytochrome c-552 of the bacterium. The optimal pH of the reaction was 3.5. The enzyme also oxidized the reduced form of rusticyanin, a copper protein of the bacterium. Our results indicate that the reduction of molecular oxygen by this enzyme may occur in the periplasm.     

Solubilization and speciation of iron during pyrite oxidation by Thiobacillus ferrooxidans

Various species of soluble iron in pyrite‐grown cultures of Thiobacillus ferrooxidans were determined by colorimetry, atomic absorption spectrometry, and ultraviolet spectroscopy. All the cultures were incubated for six weeks before iron analysis. The effects of the following factors were investigated: particle size, initial pH, shaking (aeration), concentration of pyrite, and concentration of yeast extract. Shaking, but not initial pH nor particle size, influenced the relative proportion of different iron species. Polynomial regressions could be used to describe the functional relationship between the different iron species and concentration of pyrite; fewer relationships were evident with respect to concentration of yeast extract. The variance‐covariance matrices indicated a linear dependence among the different iron species. Canonical correlations indicated perfect correlations between group variables of iron, copper, and zinc, with the exception of an absence of significant correlation with the hydroxy complex of iron (FeOH²⁺).

The dissolved ferrous iron (dissociated and weakly chelated) always remained less than 7% of the total iron in solution. The total ferrous iron, which included complexed species, amounted to 7–34% of the total iron in solution. The concentrations of dissociated ferrous and ferric iron and their weak chelates (the dissolved iron) remained mostly constant, irrespective of the concentration of the total iron in solution. Most of the total iron was complexed as ferric species and the amount correlated with culture conditions. The hydroxy complex (FeOH²⁺), which was indicative of the relative amount of hydrolyzable ferric iron upon dilution in CO₂‐free water, usually ranged between 60 and 80% of the total iron. The amount of the total iron in uninoculated controls was less than 12% of that solu‐bilized in the presence of iron‐oxidizing thiobacilli.

T. ferrooxidans was enumerated by a most‐probable‐number technique after three and six weeks of growth on pyrite. The counts after three weeks indicated an increase in the number of free and loosely attached bacteria, followed by a decline of about one order of magnitude in bacterial numbers after six weeks. The technique for bacterial enumeration was deemed unsatisfactory because it could not account for cells attached on pyrite.     

Use of Thiobacillus ferrooxidans for iron oxidation and precipitation

Fe(II) oxidation reaction was carried out using an acidophilic microorganism, Thiobacillus ferrooxidans. Four different parameters such as pH, Fe(II), Fe(III) and biomass concentration were studied. The oxida-tion reaction follows a pseudo first order rate equation. Apparent reaction rate constants were calculated. Unified rate equation was developed using the four parameters. Along with oxidation, a part of the iron also was precipitated. The extent of Fe(III) precipitation in each case was calculated. © Rapid Science 1998     

A kinetic model for biological oxidation of ferrous iron by Thiobacillus ferrooxidans

The kinetics of bacterial oxidation of ferrous iron in the presence of Thiobacillus ferrooxidans cells were studied using an initial-rate method. Measurements of the redox potential of the solution during the oxidation of ferrous iron were used to assess the initial rate of the reaction. Effects on the rate of reaction were determined for ferrous iron concentration in the range 0.25 to 30 kg m(-3), bacterial concentration in the range 3.25 x 10(7) to 4.47 x 10(8) cells mL(-1), and temperature in the range 20 to 35 degrees C. Using these experimental results and an approach based on Michaelis-Menten kinetics, a model for biological oxidation of ferrous iron was developed. The model, which incorporates terms for the effect of temperature and substrate and cell inhibition, was successfully used to simulate the full range of experimental data obtained. (c) 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 53: 478-486, 1997.     

Thiobacillus ferrooxidans cytochrome c oxidase: purification, and molecular and enzymatic features.

Cytochrome c oxidase from Thiobacillus ferrooxidans was purified to homogeneity and some of its properties were studied. The oxidase was solubilized with n-octyl-beta-D-thioglucoside (OTG) under acidic conditions (pH 4.0) and purified by one step of ion-exchange chromatography with a CM-Toyopearl column. The absorption spectrum of the oxidase showed peaks at 420 and 595 nm in the oxidized form and at 440 and 595 nm in the reduced form. Its CO compound showed a novel absorption spectrum; a double-peaked gamma band appeared at 429 and 438 nm. The oxidase seemed to have CuA-like copper atom from its ESR and near-infrared spectra. The oxidase molecule consisted of three polypeptides with molecular weights of 53,000, 22,000, and 17,000, respectively, as estimated by polyacrylamide gel electrophoresis in the presence of sodium dodecyl sulfate. The molecular weight of the enzyme in a solution containing detergents was estimated to be 169,000 on the basis of the results obtained by gel filtration, while the molecular weight per heme alpha was estimated to be 83,700. The copper content of the oxidase was 1.01 g atom per mol of heme alpha. Therefore, the cytochrome seemed to contain one molecule of heme alpha and one atom of copper in the minimal structural unit consisting of one molecule each of the three subunits, and to occur as a dimer of the unit in the solution. The oxidase oxidized ferrocytochrome c-552 of the bacterium, and the optimal pH of the reaction was 3.5.(ABSTRACT TRUNCATED AT 250 WORDS)     

Ferric iron reduction by Thiobacillus ferrooxidans at extremely low pH-values

When ferrous iron and sulfur were supplied, cells of T. ferrooxidans in a well-aerated medium started growth by oxidizing ferrous iron. After ferrous iron depletion a lagphase followed before sulfur oxidation started. During sulfur oxidation at pH-values below 1.3 (±0,2) the ferrous iron concentration increased again, although the oxygen saturation of the medium amounted to more than 95%. The number of viable cells did not increase. Thus resting cells of T. ferrooxidans, which are oxidizing sulfur to maintain their proton balance, reduce ferric to ferrous iron. The ferrous iron-oxidizing system seemed to be inhibited at pH-values below 1.3. At a pH-value of 1.8 the ferrous iron was reoxidized at once. A scheme for the linkage of iron- and sulfur metabolism is discussed.     

Occurrences at mineral-bacteria interface during oxidation of arsenopyrite by Thiobacillus ferrooxidans

The combination of an improved bacterial desorption method, scanning electron microscopy (SEM), diffuse reflectance and transmission infrared Fourier transform spectroscopy, and a desorption-leaching device like high-pressure liquid chromatography (HPLC) was used to analyze bacterial populations (adhering and free bacteria) and surface-oxidized phases (ferric arsenates and elemental sulfur) during the arsenopyrite biooxidation by Thiobacillus ferrooxidans. The bacterial distribution, the physicochemical composition of the leachate, the evolution of corrosion patterns, and the nature and amount of the surface-oxidized chemical species characterized different behavior for each step of arsenopyrite bioleaching. The first step is characterized by a slow but strong adhesion of bacteria to mineral surfaces, the appearance of a surface phase of elemental sulfur, the weak solubilization of Fe(II), As(III), and As(V), and the presence of the first corrosion patterns, which follow the fragility zones and the crystallographic orientation of mineral grains. After this short step, growth of the unattached bacteria begins, while ferrous ions in solution are oxidized by them. Ferric ions produced by the bacteria can oxidize the sulfide directly and are regenerated by Fe(II) bacterial oxidation. At this time, a bioleaching cycle takes place and a coarse surface phase of ferric arsenate (FeAsO(4) . xH(2)O where x approximately 2) and deep ovoid pores appear. At the end of the bioleaching cycle, the high concentration of Fe(III) and As(V) in solution promotes the precipitation of a second phase of amorphous ferric arsenate (FeAsO(4) . xH(2)O where x approximately 4) in the leachate. Then the biooxidation process ceases: The bacteria adhering to the mineral sufaces are coated by the ferric arsenates and the concentration of Fe(III) on the leachate is found to have decreased greatly. Both oxidation mechanisms (direct and indirect oxidation) have been stopped. (c) 1995 John Wiley & Sons, Inc.     

Inhibition of growth, iron, and sulfur oxidation in Thiobacillus ferrooxidans by simple organic compounds.

Iron and sulfur oxidation by Thiobacillus ferrooxidans as well as growth on ferrous iron were inhibited by a variety of low molecular weight organic compounds. The influences of chemical structure of the organic inhibitors, pH, temperature, physical treatment of cells, and added inhibitory or stimulatory inorganic ions and iron oxidation suggest that a major factor contributing to the inhibitory effects on iron oxidation is the relative electronegativity of the organic molecule. The data also suggest that inhibitory organic compounds may (i) directly affect the iron-oxidizing enzyme system, (ii) react abiologically with ferrous iron outside the cell, (iii) interfere with the roles of phosphate and sulfate in iron oxidation, and (iv) nonselectively disrupt the cell envelope or membrane.     

The ferrous iron oxidation kinetics of Thiobacillus ferrooxidans in batch cultures

The ferrous iron oxidation kinetics of Thiobacillus ferrooxidans in batch cultures was examined, using on-line off-gas analyses to measure the oxygen and carbon dioxide consumption rates continuously. A cell suspension from continuous cultures at steady state was used as the inoculum. It was observed that a dynamic phase occurred in the initial phase of the experiment. In this phase the bacterial ferrous iron oxidation and growth were uncoupled. After about 16 h the bacteria were adapted and achieved a pseudo-steady state, in which the specific growth rate and oxygen consumption rate were coupled and their relationship was described by the Pirt equation. In pseudo-steady state, the growth and oxidation kinetics were accurately described by the rate equation for competitive product inhibition. Bacterial substrate consumption is regarded as the primary process, which is described by the equation for competitive product inhibition. Subsequently the kinetic equation for the specific growth rate, μ, is derived by applying the Pirt equation for bacterial substrate consumption and growth. The maximum specific growth rate, μ _max, measured in the batch culture agrees with the dilution rate at which washout occurs in continuous cultures. The maximum oxygen consumption rate, q _O2,max, of the cell suspension in the batch culture was determined by respiration measurements in a biological oxygen monitor at excess ferrous iron, and showed changes of up to 20% during the course of the experiment. The kinetic constants determined in the batch culture slightly differ from those in continuous cultures, such that, at equal ferric to ferrous iron concentration ratios, biomass-specific rates are up to 1.3 times higher in continuous cultures. Received: 8 February 1999 / Accepted: 17 February 1999     

Sulfide oxidation by spheroplasts of Thiobacillus ferrooxidans.

Thiobacillus ferrooxidans is an acidophilic organism important to metal leaching of low-grade ores. The aforementioned importance is related to the ability of the bacterium to oxidize reduced iron and sulfur, principally found in nature as pyrite (FeS2). The present study dealt with sulfide oxidation at low pH values and the involvement of the cell envelope in the process of the inorganic oxidations. Sulfide oxidation was noted in spheroplasts of T. ferrooxidans prepared by enzymatic and chemical treatments and partially purified by differential centrifugation. No enzyme activities were noted in membrane fractions containing enrichments of lipopolysaccharide symbolic of outer membrane material or in membrane vesicles containing (or associated with) higher levels of proteins. Results to date indicate that in an acid milieu the envelope structure containing both the outer membrane and the intact inner cytoplasmic membrane is required for sulfide oxidation.     

Mathematical model of the oxidation of ferrous iron by a biofilm of Thiobacillus ferrooxidans

Microbial oxidation of ferrous iron may be a viable alternative method of producing ferric sulfate, which is a reagent used for removal of H(2)S from biogas. The paper introduces a kinetic study of the biological oxidation of ferrous iron by Thiobacillus ferrooxidans immobilized on biomass support particles (BSP) composed of polyurethane foam. On the basis of the data obtained, a mathematical model for the bioreactor was subsequently developed. In the model described here, the microorganisms adhere by reversible physical adsorption to the ferric precipitates that are formed on the BSP. The model can also be considered as an expression for the erosion of microorganisms immobilized due to the agitation of the medium by aeration.     

Stannous and cuprous ion oxidation by Thiobacillus ferrooxidans.

Oxidation of stannous chloride by Thiobacillus ferrooxidans was studied manometrically. At low stannous ion concentrations, initial oxidation rate was proportional to concentration. Optimum pH for oxidation was 2.3 optimum temperature was 37-40 degrees C. Spectrophotometry showed reduction of cytochromes in suspensions of whole cells on addition of ferrous, stannous, or cuprous salts. Cytochrome c reductase activity in cell-free extracts was assayed with ferrous, stannous, or cuprous ions as electron donors. It appears unlikely that an essential non-biological reaction, the reduction of ferric ions by stannous or cuprous ions, is involved. Growth of T. ferrooxidans was not obtained with either stannous chloride or stannous sulphate as sole energy source.     

Tryptophan 334 oxidation in bovine cytochrome c oxidase subunit I involves free radical migration

A single tryptophan (W(334(I))) within the mitochondrial-encoded core subunits of cytochrome c oxidase (CcO) is selectively oxidized when hydrogen peroxide reacts with the binuclear center. W(334(I)) is converted to hydroxytryptophan as identified by reversed-phase HPLC-electrospray ionization tandem mass spectrometry analysis of peptides derived from the three SDS-PAGE purified subunits. Total sequence coverage of subunits I, II and III was limited to 84%, 66% and 54%, respectively. W(334(I)) is located on the surface of CcO at the membrane interface. Two other surface tryptophans within nuclear-encoded subunits, W(48(IV)) and W(19(VIIc)), are also oxidized when hydrogen peroxide reacts with the binuclear center (Musatov et al. (2004) Biochemistry 43, 1003-1009). Two aromatic-rich networks of amino acids were identified that link the binuclear center to the three oxidized tryptophans. We propose the following mechanism to explain these results. Electron transfer through the aromatic networks moves the free radicals generated at the binuclear center to the surface-exposed tryptophans, where they produce hydroxytryptophan.