Molybdenum Oxidation by Thiobacillus ferrooxidans

Thiobacillus ferrooxidans AP19-3 oxidized molybdenum blue (Mo⁵⁺) enzymatically. Molybdenum oxidase in the plasma membrane of this bacterium was purified ca. 77-fold compared with molybdenum oxidase in cell extract. A purified molybdenum oxidase showed characteristic absorption maxima due to reduced-type cytochrome oxidase at 438 and 595 nm but did not show absorption peaks specific for c-type cytochrome. The optimum pH of molybdenum oxidase was 5.5. The activity of molybdenum oxidase was completely inhibited by sodium cyanide (5 mM) or carbon monoxide, and an oxidized type of cytochrome oxidase in a purified molybdenum oxidase was reduced by molybdenum blue, indicating that cytochrome oxidase in the enzyme plays a crucial role in molybdenum blue oxidation.     

氧化亚铁硫杆菌的形态及对Fe2+的氧化研究

在纯培养的条件下,对江西德兴铜矿酸性矿坑水中分离出的一株氧化亚铁硫杆菌(Thiobacillus ferrooxidans)的细胞形态、生长条件以及对Fe2 的氧化进行了初步研究。透射电子显微镜检查的结果表明,其成熟菌体大小均一,有较好的运动性;采用光学显微镜对微生物进行菌群观测和利用血小板计数器法对细菌计数的结果表明,在摇床转速为160r/min的条件下,T.f.菌在9K液体培养基中最适生长条件为温度30℃左右,最佳初始pH 2.0;用重铬酸钾滴定法测定铁的结果表明,在摇床转速为160r/min的条件下,pH值1.7,温度30℃时T.f.菌对Fe2 的氧化速率最大,约为0.58g/L·h。     

Combined degradation of covellite by Thiobacillus thiooxidans and Thiobacillus ferrooxidans

Summary In the presence of iron, which is always associated with natural sulphide ores, the percentages of copper dissolution in the bioleaching of covellite were 34 and 45 % when Thiobacillus thiooxidans and Thiobacillus ferrooxidans were used together and when an indirect bioleaching with attached bacteria was performed respectively. In the latter, the percentage of copper dissolution was still higher than the percentages obtained with pure cultures (36 % with a T. thiooxidans culture and 40 % with a T. ferrooxidans culture).     

Direct zinc sulphide bioleaching by Thiobacillus ferrooxidans and Thiobacillus thiooxidans

Summary Direct bioleaching (no iron(II) present) by Thiobacillus ferrooxidans mainly occurs on the surface of the very insoluble sulphides but is more important in solution when the sulphides are more soluble. In this case, Thiobacillus thiooxidans, normally not able to leach directly insoluble sulphides, has an effective leaching action.     

Biosorption of Cu by Thiobacillus ferrooxidans

Current technologies for removal and recovery of both toxic and industrial interest metals usually produce wastes with high concentrations of those substances. They are an important source of environmental pollution, specially when they contain heavy metals. This is one of the most important environmental problems, and of the most difficult to solve. So far, there have been a number of studies considering the possibility of removing and recovering heavy metals from diluted solutions. These are due, principally, because of the commercial value of some metals as well as the environmental impact caused by them. The traditional methods for removing have several disadvantages when metals are present in concentrations lower than 100?mg/l. Biosorption, which uses biological materials as adsorbents, has been considered as an alternative method. In this work, several variables that affect the capacity for copper biosorption by T. ferrooxidans have been studied. Particularly, the effect of pH, chemical pretreatment, biomass concentration and temperature have been considered. Results indicate that a capacity as high as 119?mg of Cu/g of dry biomass can be obtained at a temperature of 25?°C.     

Reduction of dichromate by Thiobacillus ferrooxidans

Chromium(VI) was reduced by Thiobacillus ferrooxidans grown with elemental sulphur as the sole energy source. Chromium(VI) reduction (as high as 2000 M), was due to the presence of sulphite and thiosulphate, among others with high reducing power which was generated during the sulphur oxidation by the bacteria. Therefore, Thiobacillus ferrooxidans could be used to treat chromium(VI)-containing industrial effluents.     

Attachment behaviour of Thiobacillus ferrooxidans cells to refractory gold concentrate particles

In the biooxidation of minerals, cells of Thiobacillus are distributed between the surface of the particles and the liquid. This work quantifies the kinetics of attachment, the equilibrium between attached and suspended cells, and the influence of ferric ion and particle size on this phenomenon. The attachment kinetics were fast, the equilibrium was reached in 10 to 30 minutes, depending on the initial population. The equilibrium curves showed three distinct phases, and the first two could be modelled by Langmuir equations. The maximum concentration of attached cells increases with the addition of ferric ions and decreases with particle size.     

Biochemical rust removal by Thiobacillus ferrooxidans

Summary Biochemical removal of rust from iron surfaces has been investigated. By immersing a rusted iron plate in the culture medium of an iron-oxidizing bacterium, Thiobacillus ferrooxidans, iron adjacent to the rust was dissolved and the rust was peeled off. Since the amount of dissolved iron per unit iron plate surface area correlated with the concentration of ferric iron in the culture medium, the formation of ferric iron is probably involved in dissolving the iron as is the case for bacterial leaching. In the present study, rust removal in a “continuous” system in which the culture medium was circulated from the fermentor to the rust removal vessel and back again to the fermentor, has also been investigated. Although growth inhibition was observed with the formation of ferric iron precipitates during the operation in this system, it was possible to prevent this precipitation by lowering the pH of the medium during the mixed cultivation of T. ferrooxidans and a sulfur-oxidizing bacterium, T. thiooxidans.     

Bacterial dissolution of pyrite by Thiobacillus ferrooxidans

The kinetics of the dissolution of pure pyrite (FeS₂) particles by Thiobacillus ferrooxidans were studied both theoretically and experimentally. Adsorption and dissolution experiments were carried out at 30 °C and pH=2, by using a batch reactor. The adsorption process of T. ferrooxidans to pyrite surface was rapid in comparison with the bacterial dissolution process. The experimental results for the adsorption equilibrium were well correlated by the Langmuir type isotherm. The growth rate of adsorbed bacteria was found to be proportional to the product of the number of adsorbed cells and the fraction of solid surface unoccupied by cells. A new kinetic model for the bacterial dissolution was presented, and shown to correlate well with the experimental data for the rate of bacterial dissolution and for the time variation in the number of cells in the liquid phase. The specific growth rate of adsorbed bacteria was also evaluated.List of Symbols f weight fraction of iron in pyrite - K _A m³/cells equilibrium constant for cell adsorption - R _A cells/d m³-mixture growth rate of bacteria adsorbed on solid surface - R _L cells/d m³-mixture growth rate of free bacteria in the liquid phase - t d time - V m³ volume of solid-liquid mixture - W kg weight of pyrite - W ₀ kg initial weight of pyrite - X _A cells/kg-solid number of adsorbed cells on solid surface - X _Am cells/kg-solid maximum adsorption capacity - X _L cells/m³-liquid number of free cells existing in the liquid phase - X _T cells/m³-mixture total number of cells - X _TO cells/m³ initial total number of cells - Y _A cells/kg-FeS₂ growth yield of adsorbed bacteria - Y _L cells/kg-Fe²⁺ growth yield of free bacteria - [Fe] _T kg/m³-liquid concentration of total iron in the liquid phase - fraction of pyrite dissolved - _V fraction of adsorption sites unoccupied by cells - _A d^–1 specific growth rate of adsorbed bacteria - _L d^–1 specific growth rate of free bacteria - volume fraction of solid particles in solid-liquid mixture     

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.     

Anaerobic leaching of covellite by Thiobacillus ferrooxidans

Thiobacillus ferrooxidans was able to grow under anaerobic conditions on copper sulphide with ferric ion as the electron acceptor. The dissolution of covellite under these conditions (68% after 35 days) was higher than values observed aerobically in cultures with similar media composition and almost as high as under aerobic conditions without iron. From these results we propose a mechanism for anaerobic bioleaching of covellite in the presence of ferric iron and speculate that it may occur in leach dumps where the oxygen concentration is, as reported elsewhere, very low. Received: 3 September 1996 / Received revision: 13 January 1997 / Accepted: 24 January 1997     

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.     

Oxidation of gallium sulfides by Thiobacillus ferrooxidans.

The bacterial oxidation of naturally occurring gallium-bearing chalcopyrite concentrate and a pure synthetic gallium (III) sulfide has been investigated at pH 1.8 and 35 degree C, using an active culture of Thiobacillus ferrooxidans. This oxidation process may proceed by direct or by indirect bacterial action. The highest dissolved gallium and copper concentrations were about 2.2 and 40.2 g/l, respectively. The order of the specific rate of oxygen uptake by T. ferrooxidans in approximately CuFES2 greater than or equal to gallium-bearing CuFeS2 greater than FeS2 greater than Cu2S greater than Cu2S greater than Ga2S3.     

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.     

Inhibition of Thiobacillus ferrooxidans by mineral flotation reagents

Summary Ferrous-iron oxidation by Thiobacillus ferrooxidans was inhibited by a number of mineral flotation reagents. Dowfroth 250 and sodium butylxanthate were the least toxic reagents studied.