Synthesis of an Iron-Oxidizing System during Growth of Thiobacillus ferrooxidans on Sulfur-Basal Salts Medium

It was found that the de novo synthesis of not only sulfur:ferric ion oxidoreductase (ferric ion-reducing system) but also iron oxidase was absolutely required when Thiobacillus ferrooxidans AP19-3 was grown on sulfur-salts medium. The results strongly suggest that iron oxidase is involved in sulfur oxidation. This bacterium could not grow on sulfur-salts medium under anaerobic conditions with Fe³⁺ as a terminal electron acceptor, suggesting that energy conservation by electron transfer between elemental sulfur and Fe³⁺ is not available for this bacterium.     

Reduction of Cupric Ions with Elemental Sulfur by Thiobacillus ferrooxidans

In anaerobic or aerobic conditions in the presence of 5 mM sodium cyanide, an inhibitor of iron oxidase, cupric ion (Cu²⁺) was reduced enzymatically with elemental sulfur (S⁰) by washed intact cells of Thiobacillus ferrooxidans AP19-3 to give cuprous ion (Cu⁺). The rate of Cu²⁺ reduction was proportional to the concentrations of S⁰ and Cu²⁺ added to the reaction mixture. The pH optimum for the cupric ion-reducing system was 5.0, and the activity was completely destroyed by 10-min incubation of cells at 70°C. The activity of Cu²⁺ reduction with S⁰ by this strain was strongly inhibited by inhibitors of hydrogen sulfide: ferric ion oxidoreductase (SFORase), such as α,α′-dipyridyl, 4,5-dihydroxy-m-benzene disulfonic acid disodium salts, and diazine dicarboxylic acid bis-(N, N-dimethylamide). A SFORase purified from this strain, which catalyzes oxidation of both hydrogen sulfide and S⁰ with Fe³⁺ or Mo⁶⁺ as an electron acceptor in the presence of glutathione, catalyzed a reduction of Cu²⁺ by S⁰, and the Michaelis constant of SFORase for Cu²⁺ was 7.2 mM, indicating that a SFORase catalyzes the reduction of not only Fe³⁺ and Mo⁶⁺ but also Cu²⁺.     

Inhibition of Sulfur Use by Sulfite Ion in Thiobacillus ferrooxidans

In Thiobacillus ferrooxidans AP19-3, elemental sulfur is oxidized by the cooperation of three enzymes, namely, hydrogen sulfide: ferric ion oxidoreductase (SFORase), sulfite: ferric ion oxidoreductase, and iron oxidase. Sulfite ions are one of the products when elemental sulfur is oxidized by SFORase. Under the conditions in which sulfite ions are accumulated in the cells, use of sulfur as an energy source by this strain was strongly inhibited. So the mechanism of inhibition by sulfite ions in T. ferrooxidans AP19-3 was studied. The activities of SFORase and iron oxidase were completely inhibited by 0.8 mm and 1.5 mm NaHSO₃, respectively. ¹⁴CO₂ uptake into washed intact cells was also completely inhibited by 1mm NaHSO₃ when ferrous ion or elemental sulfur was used as an energy source. However, the activities of ribulose-1,5-bisphosphate carboxylase, phosphoribulokinase, and ribosephosphate isomerase measured with a cell-free extract were not inhibited by NaHSO₃ at 1 mm, indicating that sulfite ions didn’t inhibit key enzymes of the Calvin cycle. Since the activity of CO₂ uptake into washed intact cells was absolutely dependent on Fe^{2 +} - or S0-oxidation, mechanism of inhibition of sulfur use by sulfite ions is proposed as follows: sulfite ions inhibit SFORase and iron oxidase, as a result T. ferrooxidans AP19-3 can not obtain a carbon source for CO₂ fixation and stops cell growth on sulfur-salts medium.     

Ferrous Iron and Sulfur Oxidation and Ferric Iron Reduction Activities of Thiobacillus ferrooxidans Are Affected by Growth on Ferrous Iron, Sulfur, or a Sulfide Ore

Eight strains of Thiobacillus ferrooxidans (laboratory strains Tf-1 [= ATCC 13661] and Tf-2 [= ATCC 19859] and mine isolates SM-1, SM-2, SM-3, SM-4, SM-5, and SM-8) and three strains of Thiobacillus thiooxidans (laboratory strain Tt [= ATCC 8085] and mine isolates SM-6 and SM-7) were grown on ferrous iron (Fe²⁺), elemental sulfur (S⁰), or sulfide ore (Fe, Cu, and Zn). The cells were studied for their aerobic Fe²⁺ - and S⁰-oxidizing activities (O₂ consumption) and anaerobic S⁰-oxidizing activity with ferric iron (Fe³⁺) (Fe²⁺ formation). Fe²⁺-grown T. ferrooxidans cells oxidized S⁰ aerobically at a rate of 2 to 4% of the Fe²⁺ oxidation rate. The rate of anaerobic S⁰ oxidation with Fe³⁺ was equal to the aerobic oxidation rate in SM-1, SM-3, SM-4, and SM-5, but was only one-half or less that in Tf-1, Tf-2, SM-2, and SM-8. Transition from growth on Fe²⁺ to that on S⁰ produced cells with relatively undiminished Fe²⁺ oxidation activities and increased S⁰ oxidation (both aerobic and anaerobic) activities in Tf-2, SM-4, and SM-5, whereas it produced cells with dramatically reduced Fe²⁺ oxidation and anaerobic S⁰ oxidation activities in Tf-1, SM-1, SM-2, SM-3, and SM-8. Growth on ore 1 of metal-leaching Fe²⁺-grown strains and on ore 2 of all Fe²⁺-grown strains resulted in very high yields of cells with high Fe²⁺ and S⁰ oxidation (both aerobic and anaerobic) activities with similar ratios of various activities. Sulfur-grown Tf-2, SM-1, SM-4, SM-6, SM-7, and SM-8 cultures leached metals from ore 3, and Tf-2 and SM-4 cells recovered showed activity ratios similar to those of other ore-grown cells. It is concluded that all the T. ferrooxidans strains studied have the ability to produce cells with Fe²⁺ and S⁰ oxidation and Fe³⁺ reduction activities, but their levels are influenced by growth substrates and strain differences.     

Energy Transduction by Anaerobic Ferric Iron Respiration in Thiobacillus ferrooxidans

Formate-grown cells of the obligately chemolithoautotrophic acidophile Thiobacillus ferrooxidans were capable of formate- and elemental sulfur-dependent reduction of ferric iron under anaerobic conditions. Under aerobic conditions, both oxygen and ferric iron could be simultaneously used as electron acceptors. To investigate whether anaerobic ferric iron respiration by T. ferrooxidans is an energy-transducing process, uptake of amino acids was studied. Glycine uptake by starved cells did not occur in the absence of an electron donor, neither under aerobic conditions nor under anaerobic conditions. Uptake of glycine could be driven by formate- and ferrous iron-dependent oxygen uptake. Under anaerobic conditions, ferric iron respiration with the electron donors formate and elemental sulfur could energize glycine uptake. Glycine uptake was inhibited by the uncoupler 2,4-dinitrophenol. The results indicate that anaerobic ferric iron respiration can contribute to the energy budget of T. ferrooxidans.     

Competitive Inhibition of Ferrous Iron Oxidation by Thiobacillus ferrooxidans by Increasing Concentrations of Cells

The oxidation of ferrous iron (Fe²⁺) to ferric iron (Fe³⁺) with dioxygen (O₂) by various strains of Thiobacillus ferrooxidans was studied by measuring the rate of O₂ consumption at various Fe²⁺ concentrations and cell concentrations. The apparent K_m values for Fe²⁺ remained constant at different cell concentrations of laboratory strains ATCC 13661 and ATCC 19859 but increased with increasing cell concentrations of mine isolates SM-4 and SM-5. The latter results are explained by the competitive inhibition of the Fe²⁺-binding site of a cell by other cells in the reaction mixture. Possible mechanisms involving cell surface properties are discussed.     

Role of Ferrous Ions in Synthetic Cobaltous Sulfide Leaching of Thiobacillus ferrooxidans

Microbiological leaching of synthetic cobaltous sulfide (CoS) was investigated with a pure strain of Thiobacillus ferroxidans. The strain could not grow on CoS-salts medium in the absence of ferrous ions (Fe²⁺). However, in CoS-salts medium supplemented with 18 mM Fe²⁺, the strain utilized both Fe²⁺ and the sulfur moiety in CoS for growth, resulting in an enhanced solubilization of Co²⁺. Cell growth on sulfur-salts medium was strongly inhibited by Co²⁺, and this inhibition was completely protected by Fe²⁺. Cobalt-resistant cells, obtained by subculturing the strain in medium supplemented with both Fe²⁺ and Co²⁺, brought a marked decrease in the amount of Fe²⁺ absolutely required for cell growth on CoS-salts medium. As one mechanism of protection by Fe²⁺, it is proposed that the strain utilizes one part of Fe²⁺ externally added to CoS-salts medium to synthesize the cobalt-resistant system. Since a similar protective effect by Fe²⁺ was also observed for cell inhibition by stannous, nickel, zinc, silver, and mercuric ions, a new role of Fe²⁺ in bacterial leaching in T. ferrooxidans is proposed.     

The effect of different Fe2+ concentrations in culture media on the recycling of ground tyre rubber by Acidithiobacillus ferrooxidans YT-1

Waste rubber has posed challenging environmental and disposal problems across the world. This study focused on the microbial reclaiming of ground tyre rubber (GTR) by Acidithiobacillus ferrooxidans YT-1 cultured in media with variable Fe²⁺ concentrations. The Acidithiobacillus ferrooxidans YT-1 strain with the ability of oxidizing sulfur and reclaiming waste rubber was isolated and identified. Toxicity tests of different rubber and additives in tyre rubber compounds to microorganisms was quantitatively investigated. After desulfurization, there were many small colonies on the surface of the desulfurizated GTR (DGTR), due to surface degradation by A. ferrooxidans YT-1. The amount of small colonies increased and sulfur content decreased with the increase of Fe²⁺ concentrations in the media, implying that Fe²⁺ concentration had a great influence on the degradation ability of A. ferrooxidans YT-1. A medium with a high Fe²⁺ concentration was good for growth of A. ferrooxidans YT-1. Compared with styrene butadiene rubber (SBR)/GTR blends, the tensile strength and elongation at the break of the SBR/DGTR blends were significantly improved. The scanning electron microscope (SEM) photographs of the fracture surface further indicated a good coherency between DGTR and the SBR matrix. These results revealed that A. ferrooxidans YT-1 cultured in a medium with a high Fe²⁺ concentration could improve the reclaiming efficiency of waste rubber.     

Ferric Iron Reduction by Acidophilic Heterotrophic Bacteria

Fifty mesophilic and five moderately thermophilic strains of acidophilic heterotrophic bacteria were tested for the ability to reduce ferric iron in liquid and solid media under aerobic conditions; about 40% of the mesophiles (but none of the moderate thermophiles) displayed at least some capacity to reduce iron. Both rates and extents of ferric iron reduction were highly strain dependent. No acidophilic heterotroph reduced nitrate or sulfate, and (limited) reduction of manganese(IV) was noted in only one strain (Acidiphilium facilis), an acidophile which did not reduce iron. Insoluble forms of ferric iron, both amorphous and crystalline, were reduced, as well as soluble iron. There was evidence that, in at least some acidophilic heterotrophs, iron reduction was enzymically mediated and that ferric iron could act as a terminal electron acceptor. In anaerobically incubated cultures, bacterial biomass increased with increasing concentrations of ferric but not ferrous iron. Mixed cultures of Thiobacillus ferrooxidans or Leptospirillum ferrooxidans and an acidophilic heterotroph (SJH) produced sequences of iron cycling in ferrous iron-glucose media.     

Active Transport of Iron in Bacillus megaterium: Role of Secondary Hydroxamic Acids

Kinetics of radioactive iron transport were examined in three strains of Bacillus megaterium. In strain ATCC 19213, which secretes the ferric-chelating secondary hydroxamic acid schizokinen, ⁵⁹Fe³⁺ uptake from ⁵⁹FeCl₃ or the ferric hydroxamate Desferal-⁵⁹Fe³⁺ was rapid and reached saturation within 3 min. In strain SK11, which does not secrete schizokinen, transport from ⁵⁹FeCl₃ was markedly reduced; the two ferric hydroxamates Desferal-⁵⁹Fe³⁺ or schizokinen-⁵⁹Fe³⁺ increased both total ⁵⁹Fe³⁺ uptake and the ⁵⁹Fe³⁺ appearing in a cellular trichloroacetic acid-insoluble fraction, although 10 min was required to reach saturation. Certain characteristics of transport from both ferric hydroxamates and FeCl₃ suggest that iron uptake was an active process. The growth-inhibitory effect of aluminum on strain SK11 was probably due to the formation of nonutilizable iron-aluminum complexes which blocked uptake from ⁵⁹FeCl₃. Desferal or schizokinen prevented this blockage. A strain (ARD-1) resistant to the ferric hydroxamate antibiotic A22765 was isolated from strain SK11. Strain ARD-1 failed to grow with Desferal-Fe³⁺ as an iron source, and it was unable to incorporate ⁵⁹Fe³⁺ from this source. Growth and iron uptake in strain ARD-1 were similar to strain SK11 with schizokinen-Fe³⁺ or the iron salt as sources. It is suggested that the ferric hydroxamates, or the iron they chelate, may be transported by a special system which might be selective for certain ferric hydroxamates. Strain ARD-1 may be unable to recognize both the antibiotic A22765 and the structurally similar chelate Desferal-Fe³⁺, while retaining its capacity to utilize schizokinen-Fe³⁺.     

Fast Kinetics of Fe2+ Oxidation in Packed-Bed Reactors

Thiobacillus ferrooxidans was used in fixed-film bioreactors to oxidize ferrous sulfate to ferric sulfate. Glass beads, ion-exchange resin, and activated-carbon particles were tested as support matrix materials. Activated carbon was tested in both a packed-bed bioreactor and a fluidized-bed bioreactor; the other matrix materials were used in packed-bed reactors. Activated carbon displayed the most suitable characteristics for use as a support matrix of T. ferrooxidans fixed-film formation. The reactors were operated within a pH range of 1.35 to 1.5, which effectively reduced the amount of ferric iron precipitation and eliminated diffusion control of mass transfer due to precipitation. The activated-carbon packed-bed reactor displayed the most favorable biomass holdup and kinetic performance related to ferrous sulfate oxidation. The fastest kinetic performance achieved with the activated-carbon packed-bed bioreactor was 78 g of Fe²⁺ oxidized per liter per h (1,400 mmol of Fe²⁺ oxidized per liter per h) at a true dilution rate of 40/h, which represents a hydraulic retention time of 1.5 min.     

Purification and some properties of sulfur:ferric ion oxidoreductase from Thiobacillus ferrooxidans.

A sulfur:ferric ion oxidoreductase that utilizes ferric ion (Fe3+) as an electron acceptor of elemental sulfur was purified from iron-grown Thiobacillus ferrooxidans to an electrophoretically homogeneous state. Under anaerobic conditions in the presence of Fe3+, the enzyme reduced 4 mol of Fe3+ with 1 mol of elemental sulfur to give 4 mol of Fe2+ and 1 mol of sulfite, indicating that it corresponds to a ferric ion-reducing system (T. Sugio, C. Domatsu, O. Munakata, T. Tano, and K. Imai, Appl. Environ. Microbiol. 49:1401-1406, 1985). Under aerobic conditions, sulfite, but not Fe2+, was produced during the oxidation of elemental sulfur by this enzyme because the Fe2+ produced was rapidly reoxidized chemically by molecular oxygen. The possibility that Fe3+ serves as an electron acceptor under aerobic conditions was ascertained by adding o-phenanthroline, which chelates Fe2+, to the reaction mixture. Sulfur:ferric ion oxidoreductase had an apparent molecular weight of 46,000, and it is composed of two identical subunits (Mr = 23,000) as estimated by sodium dodecyl sulfate-polyacrylamide gel electrophoresis. Sulfur oxidation by this enzyme was absolutely dependent on the presence of reduced glutathione. The enzyme had an isoelectric point and a pH optimum at pH 4.6 and 6.5, respectively. Almost all the activity of sulfur:ferric ion oxidoreductase was observed in the osmotic shock fluid of the cells, suggesting that it was localized in the periplasmic space of the cells.     

Sensitivity of Iron-Oxidizing Bacteria, Thiobacillus ferrooxidans and Leptospirillum ferrooxidans, to Bisulfite Ion

When grown on iron-salt medium supplemented with the bisulfite ion, Leptospirillum ferrooxidans was much more sensitive to the ion than was Thiobacillus ferrooxidans. The causes of the sensitivity of L. ferrooxidans to the bisulfite ion were studied. The bisulfite ion completely inhibited the iron-oxidizing activities of L. ferrooxidans and T. ferrooxidans at 0.02 and 0.2 mM, respectively. A trapping reagent for the bisulfite ion, formaldehyde, completely reversed the inhibition. The treatment of intact cells with 1.0 mM bisulfite ion for 1 h and washing the bisulfite ion from the cells had no harmful effects on the iron-oxidizing activity of T. ferrooxidans. However, the treatment of L. ferrooxidans with 0.1 mM bisulfite ion for 1 h completely destroyed the iron-oxidizing activity. T. ferrooxidans had sulfite:ferric ion oxidoreductase activity. In contrast, a quite low level of sulfite:ferric ion oxidoreductase activity was found in L. ferrooxidans, suggesting that it is much more difficult for L. ferrooxidans to oxidize the bisulfite ion to the less harmful sulfate than it is for T. ferrooxidans. These results suggest that the sensitivity of L. ferrooxidans to the bisulfite ion is due to a lack of an active sulfite:ferric ion oxidoreductase and the sensitivity of its iron oxidase to bisulfite ion.     

Kinetics of Iron Oxidation by Thiobacillus ferrooxidans

A statistical relationship between the rate of ferric ion production by a strain of Thiobacillus ferrooxidans and various levels of cell concentration, Fe²⁺ concentration, Na⁺ concentration, and temperature was studied by a direct colorimetric method at 304 nm. The relationship was linear (90 to 93%), cross-product (3 to 4%), and quadratic (1 to 2%). The levels of cell concentration and Fe²⁺ concentration and their respective interactions with one another and the other factors had the most significant effects on the regression models. The solution of the quadratic response surface for optimum oxidation was a saddle point, and the predicted critical levels of temperature, cell concentration, Fe²⁺ concentration, and Na⁺ concentration ranged between −6 and 2°C, 0.43 and 0.62 mg/ml, 72 and 233 mM, and 29.6 mM, respectively.     

Isolation and Characterization of Acidithiobacillus ferrooxidans Strain D3-2 Active in Copper Bioleaching from a Copper Mine in Chile

Acidithiobacillus ferrooxidans strain D3-2, which has a high copper bioleaching activity, was isolated from a low-grade sulfide ore dump in Chile. The amounts of Cu²⁺ solubilized from 1% chalcopyrite (CuFeS₂) concentrate medium (pH 2.5) by A. ferrooxidans strains D3-2, D3-6, and ATCC 23270 and 33020 were 1360, 1080, 650, and 600 mg·l ^?1·30 d^?1. The iron oxidase activities of D3-2, D3-6, and ATCC 23270 were 11.7, 13.2, and 27.9 μl O₂ uptake·mg protein^?1·min^?1. In contrast, the sulfite oxidase activities of strains D3-2, D3-6, and ATCC 23270 were 5.8, 2.9, and 1.0 μl O₂ uptake·mg protein^?1·min^?1. Both of cell growth and Cu-bioleaching activity of strains D3-6 and ATCC 23270, but not, of D3-2, in the chalcopyrite concentrate medium were completely inhibited in the presence of 5 mM sodium bisulfite. The sulfite oxidase of strain D3-2 was much more resistant to sulfite ion than that of strain ATCC 23270. Since sulfite ion is a highly toxic intermediate produced during sulfur oxidation that strongly inhibits iron oxidase activity, these results confirm that strain D3-2, with a unique sulfite resistant-sulfite oxidase, was able to solubilize more copper from chalcopyrite than strain ATCC 23270, with a sulfite-sensitive sulfite oxidase.     

Anaerobic Growth of Thiobacillus ferrooxidans

The obligately autotrophic acidophile Thiobacillus ferrooxidans was grown on elemental sulfur in anaerobic batch cultures, using ferric iron as an electron acceptor. During anaerobic growth, ferric iron present in the growth media was quantitatively reduced to ferrous iron. The doubling time in anaerobic cultures was approximately 24 h. Anaerobic growth did not occur in the absence of elemental sulfur or ferric iron. During growth, a linear relationship existed between the concentration of ferrous iron accumulated in the cultures and the cell density. The results suggest that ferric iron may be an important electron acceptor for the oxidation of sulfur compounds in acidic environments.     

Role of Thiobacillus ferrooxidans and sulphur (sulphide)-dependent ferric-ion-reducing activity in the oxidation of sulphide minerals

 Thiobacillus ferrooxidans oxidized the sulphide minerals e.g., pyrite, pyrrhotite and copper concentrate under anaerobic conditions in the presence of ferric ion as sole electron acceptor. Copper and iron were solubilized from sulphide ores by the sulphur (sulphide)-dependent ferric-ion oxidoreductase activity. Treatment of resting cells of T. ferrooxidans with 0.5% phenol for 30 min completely destroyed the iron- and copper-solubilizing activity. The above treatment destroyed the sulphur(sulphide)-dependent ferric-ion-reducing activity completely but did not affect the iron-oxidizing activity. The results suggest that sulphur(sulphide)-dependent ferric-ion-reducing activity actively participates in the oxidation of sulphide minerals under anaerobic conditions. The activity of sulphur(sulphide)-dependent ferric ion reduction in the solubilization of iron and copper from the sulphide ores were also observed under aerobic conditions in presence of sodium azide (0.1 μmol), which completely inhibits the iron-oxidizing activity. Received: 23 May 1995/Received revision: 10 October 1995/Accepted: 16 October 1995     

Iron uptake from ferric citrate by Vibrio anguillarum

We report here that Vibrio anguillarum possesses a non-inducible active transport system which can efficiently supply iron to the cell from ferric citrate, independently of the siderophore-based mechanisms. The strains tested were able to grow in CM9 medium in iron-restricted conditions when ferric citrate was present in the medium. Moreover, the presence of ferric citrate inhibited the production of siderophores in the strains tested. V. anguillarum cells and isolated membranes could incorporate ⁵⁵Fe³⁺ complexed by citrate, without a difference between cells grown in the presence or absence of ferric citrate. The presence of 2,4-dinitrophenol, ferrozine, ferricyanide, trypsin, as well as low temperature produced a marked decrease or total inhibition of ⁵⁵Fe³⁺ uptake by the cells. All these results suggest that iron uptake from ferric citrate in V. anguillarum must be an energy-dependent process not induced by the presence of iron or citrate in the medium, mediated by a membrane protein(s), which may require an iron reduction step to function.     

Degradation of massive pyrite: Physical,chemical, and bacterial effects

Massive pyrite was shown to produce soluble iron, hydrogen, and sulfate ions on exposure to air and water. The rate of this process was directly proportional to the surface area of the mineral; it was unaffected by a drop in the pH and the presence of the ferrous and sulfate ions formed. Cupic ion had no effect but ferric ion accelerated pyrite degradation until all the ferric ion was consumed, in accordance with FeS₂ + 2Fe³⁺ —>‐3Fe²⁺ + 2S°. Thiobacillus ferrooxidans increased pyrite degradation considerably; the presence of Thiobacillus thiooxidans had no influence on pyrite degradation.