Effect of particle-particle shearing on the bioleaching of sulfide minerals

The biological leaching of sulfide minerals, used for the production of gold, copper, zinc, cobalt, and other metals, is very often carried out in slurry bioreactors, where the shearing between sulfide particles is intensive. In order to be able to improve the efficiency of the bioleaching, it is of significant importance to know the effect of particle shearing on the rate of leaching. The recently proposed concept of ore immobilization allowed us to study the effect of particle shearing on the rate of sulfide (pyrite) leaching by Thiobacillus ferrooxidans. Using this concept, we designed two very similar bioreactors, the main difference between which was the presence and absence of particle-particle shearing. It was shown that when the oxygen mass transfer was not the rate-limiting step, the rate of bioleaching in the frictionless bioreactor was 2.5 times higher than that in a bioreactor with particle friction (shearing). The concentration of free suspended cells in the frictionless bioreactor was by orders of magnitude lower than that in the frictional bioreactor, which showed that particle friction strongly reduces the microbial attachment to sulfide surface, which, in turn, reduces the rate of bioleaching. Surprisingly, it was found that formation of a layer of insoluble iron salts on the surface of sulfide particles is much slower under shearless conditions than in the presence of particle-particle shearing. This was explained by the effect of particle friction on liquid-solid mass transfer rate. The results of this study show that reduction of the particle friction during bioleaching of sulfide minerals can bring important advantages not only by increasing significantly the bioleaching rate, but also by increasing the rate of gas-liquid oxygen mass transfer, reducing the formation of iron precipitates and reducing the energy consumption. One of the efficient methods for reduction of particle friction is ore immobilization in a porous matrix.     

Temperature Effects on Bacterial Leaching of Sulfide Minerals in Shake Flask Experiments

The microbiological leaching of a sulfide ore sample was investigated in shake flask experiments. The ore sample contained pyrite, pyrrhotite, pentlandite, sphalerite, and chalcopyrite as the main sulfide minerals. The tests were performed at eight different temperatures in the range of 4 to 37°C. The primary data were used for rate constant calculations, based on kinetic equations underlying two simplified models of leaching, i.e., a shrinking particle model and a shrinking core model. The rate constants thus derived were further used for the calculation of activation energy values for some of the sulfide minerals present in the ore sample. The chalcopyrite leaching rates were strongly influenced by the interaction of temperature, pH, and redox potential. Sphalerite leaching could be explained with the shrinking particle model. The data on pyrrhotite leaching displayed good fit with the shrinking core model. Pyrite leaching was found to agree with the shrinking particle model. Activation energies calculated from the rate of constants suggested that the rate-limiting steps were different for the sulfide minerals examined; they could be attributed to a chemical or biochemical reaction rather than to diffusion control.     

Mathematical modeling of biological sulfide removal in a fed batch bioreactor

In this study, biological sulfide removal is investigated in a fed batch bioreactor. In this process, sulfide is converted into elemental sulfur particles as an intermediate in the oxidation of hydrogen sulfide to sulfate. The main product is sulfur at low dissolved oxygen or at high sulfide concentrations and also more sulfates are produced at high dissolved oxygen. According to the carried out reactions, a mathematical model is developed. The model parameters are estimated and the model is validated by comparing with some experimental data. The results show that, the proposed model is in a good agreement with experimental data. According to the experimental result and mathematical model, sulfate and sulfur selectivity are sensitive to the concentration of dissolved oxygen. For sulfide concentration 0.2 (mM) in the bioreactor and dissolved oxygen of 0.5 ppm, only 10% of sulfide load is converted to sulfate, while it is 60% at the same sulfide concentration and dissolved oxygen of 4.5 ppm. At high sulfide load to the bioreactor, the concentration of uneliminated sulfide increases; it leads to more sulfur particle selectivity and consequently, less sulfate selectivity.     

Quantitation of labile sulfide content and P700 photochemistry in spinach photosystem I particles

Treatment of spinach photosystem I particles with 2 or 4 M urea containing 5 mM ferricyanide produces a time-dependent conversion of labile sulfide to zero-valence sulfur in the membrane-bound iron-sulfur proteins. The integrity of the primary electron donor, P700, remains intact when measured as a chemical oxidized-minus-reduced difference spectrum. The effect on the light-induced oxidation of P700 is complex; the extent of the normally-fast P700 photooxidation correlates directly with the amount of labile sulfide remaining in the particle but a slow phase of photooxidation only becomes evident in increasingly depleted particles and shows no relationship with the amount of remaining labile sulfide. The data is taken as evidence for the participation of an iron-sulfur protein in the primary photochemistry of photosystem I in green plants.     

An Improved Method for Standardization of Microspectrofluorometers

The use of meshed cadmium-zinc sulfide fluorescent particles in combination with an electron microscope locator grid greatly facilitates the standardization of miam spectrofluorometers. The fluorescent particles emit maximally at 570 nm, and the intensity of fluorescence is directly proportional to cross-sectional area when epi-illumination is used Details concerning technique and fluorescent particle characteristics are reported.     

Growth kinetics of the photosynthetic bacterium Chlorobium thiosulfatophilum in a fed-batch reactor

Hydrogen sulfide dissolved in water can be converted to elementary sulfur or sulfate by the photosynthetic bacterium Chlorobium thiosulfatophilum. Substrate inhibition occurred at sulfide concentrations above 5.7 mM. Light inhibition was found at average light intensities of 40,000 lux in a sulfide concentration of 5 mM, where no substrate inhibition occurred. Light intensity, the most important growth parameter, was attenuated through both scattering by sulfur particles and absorption by the cells. Average cell and sulfur particle sizes were 1.1 and 9.4 mum, respectively. Cells contributed 10 times as much to the turbidity as sulfur particles of the same weight concentration. The light attenuation factor was mathematically modeled, considering both the absorption and scattering effects based on the Beer-Lambert law and the Rayleigh theory, which were introduced to the cell growth model. Optimal operational conditions relating feed rate vs. light intensity were obtained to suppress the accumulation of sulfate and sulfide and save light energy for 2- and 4-L fed-batch reactors. Light intensity should be greater for the same performance (H(2)S removal rate/unit cell concentration) in larger reactors due to the scaleup effect on light transmission. Knowledge of appropriate growth kinetics in photosynthetic fed-batch reactors was essential to increase feed rate and light intensity and therefore cell growth. A mathematical model was developed that describes the cell growth by considering the light attenuation factor due to scattering and absorption and the crowding effect of the cells. This model was in good agreement with the experimental results. (c) 1992 John Wiley & Sons, Inc.     

R-phycoerythrin: a natural ligand for detoxifying cadmium ions and a tunnel matrix for synthesis of cadmium sulfide nanoparticles

As evidenced by ion-selective electrode potentiometry, the hexameric R-phycoerythrin (RPE) molecule binds 20-4000 cadmium ions (Cd2+) depending on Cd2+ concentration in the solution. Cadmium ions bound to RPE serve as nuclei of cadmium sulfide crystallization in the presence of sulfide ions. According to spectrometric, electron-microscopic and capillary electrophoresis data, the particles are heteroaggregates of 3.2 x 6 nm in size. The fact that the particle size fits the size of the central tunnel of the RPE molecule and the similarity between the electrophoretic patterns of free RPE and the RPE-CdS complex indicate that the tunnel space, limiting the crystal growth, is the most probable site of nanoparticle formation. Properties of the nanoparticles can be modified by changing temperature, pH, etc. It is concluded that RPE can be used as a reagent for detoxification of cadmium ions and a matrix for synthesis of elongated CdS nanoparticles.     

Effect of biologically produced sulfur on gas absorption in a biotechnological hydrogen sulfide removal process

Absorption of hydrogen sulfide in aqueous suspensions of biologically produced sulfur particles was studied in a batch stirred cell reactor, and in a continuous set-up, consisting of a lab-scale gas absorber column and a bioreactor. Presence of biosulfur particles was found to enhance the absorption rate of H(2)S gas in the mildly alkaline liquid. The mechanism for this enhancement was however found to depend on the type of particles used. In the gently stirred cell reactor only small hydrophilic particles were present (d(p) < 3 microm) and the enhancement of the H(2)S absorption rate can be explained from the heterogeneous reaction between dissolved H(2)S and solid elemental sulfur to polysulfide ions, S(x) (2-). Conditions favoring enhanced H(2)S absorption for these hydrophilic particles are: low liquid side mass transfer (k(L)), high sulfur content, and presence of polysulfide ions. In the set-up of gas absorber column and bioreactor, both small hydrophilic particles and larger, more hydrophobic particles were continuously produced (d(p) up to 20 microm). Here, observed enhancement could not be explained by the heterogeneous reaction between sulfide and sulfur, due to the relatively low specific particle surface area, high k(L), and low [S(x) (2-)]. A more likely explanation for enhancement here is the more hydrophobic behavior of the larger particles. A local increase of the hydrophobic sulfur particle concentration near the gas/liquid interface and specific adsorption of H(2)S at the particle surface can result in an increase in the H(2)S absorption rate.     

Glutathione-coated cadmium-sulfide crystallites in Candida glabrata

Cadmium-sulfide crystallites form in the yeast Candida glabrata cultured in the presence of cadmium salts. The particles function to sequester and detoxify intracellular cadmium ions. The crystallites are peptide-coated, but the coating peptide varies with the nutrient conditions of the growth medium. When cultured in rich nutrient broth the yeast forms intracellular CdS particles coated with a mixture of glutathione and the gamma-glutamylcysteine dipeptide. In contrast, cultures in synthetic minimal medium yield particles coated with polymerized gamma EC peptides of general structure (gamma-Glu-Cys)n-Gly. Glutathione/gamma-glutamylcysteine particles exhibit properties analogous to quantum, semiconductor-type crystallites. The optical properties are dependent on particle size, and irradiation results in photoluminescence and photoreduction not observed in bulk CdS mineral. Aerobic irradiation leads to particle decomposition presumably via oxidation of the sulfide ions within the crystallite.     

Bacterial Oxidation of Sulfide Minerals in Column Leaching Experiments at Suboptimal Temperatures

The purpose of the work was to quantitatively characterize temperature effects on the bacterial leaching of sulfide ore material containing several sulfide minerals. The leaching was tested at eight different temperatures in the range of 4 to 37°C. The experimental technique was based on column leaching of a coarsely ground (particle diameter, 0.59 to 5 mm) ore sample. The experimental data were used for kinetic analysis of chalcopyrite, sphalerite, and pyrrhotite oxidation. Chalcopyrite yielded the highest (73 kJ/mol) and pyrrhotite yielded the lowest (25 kJ/mol) activation energies. Especially with pyrrhotite, diffusion contributed to rate limitation. Arrhenius plots were also linear for the reciprocals of lag periods and for increases of redox potentials (dmV/dt). Mass balance analysis based on total S in leach residue was in agreement with the highest rate of leaching at 37 and 28°C. The presence of elemental S in leach residues was attributed to pyrrhotite oxidation.     

Sulfide assessment in bioreactors with gas replacement

Many biological processes have utilized the addition of sulfide constituents, such as sodium sulfide or cysteine-sulfide, to affect the redox potential, remove residual oxygen, and/or provide a source of sulfur for metabolism. However, the effects of sulfide constituents and associated sulfide concentrations on growth and product formation of cellular systems have shown considerable variance. In this work, models were developed that explained sulfide loss in bottle studies (batch reactors) and continuously gas-purged reactors. Since sulfide in liquid can be converted to volatile hydrogen sulfide (H₂S), mass transfer plays a key role for sulfide loss in continuous reactors, whereas equilibrium is critical for sulfide loss in batch reactors. Models of sulfide can be used to understand the fate of sulfide during an experiment and to design experiments to maintain constant sulfide levels for providing greater clarity when interpreting experimental results. Cellular experiments for ethanol/acetic acid formation from syngas were carried out to demonstrate the maintenance of constant sulfide levels of 0–1.9 mM throughout the experiment. Results showed that cell growth was slightly affected by the sulfide concentration, ethanol production was favored at higher sulfide concentrations, and acetic acid production was favored at lower sulfide concentrations.     

Laminated microbial ecosystems on sheltered beaches in Scapa Flow, Orkney Islands

Abstract Laminated microbial sediment ecosystems which develop in the upper tidal zone of Scapa Flow beaches, Orkney Islands were investigated with respect to depth profiles of chlorophyll a , bacteriochlorophyll a , pH, redox, oxygen and the following inorganic sulfur compounds: free sulfide, FeS, polysulfides, polythionates, elemental sulfur and thiosulfate. In addition, particle size distribution and light penetration were determined at all sampling locations.
Three main types of laminated sediment ecosystems were recognized, designated the 'classical' type (layer of cyanobacteria underlain by layer of purple sulfur bacteria), the 'single-layer' type (chlorophyll a containing organisms absent, purple sulfur bacteria at sediment surface), and the 'inverted' type (chlorophyll a containing organisms underlying purple sulfur bacteria). The dominant purple sulfur bacterium was Thiocapsa roseopersicina and Chromatium vinosum was observed less commonly. The principal cyanobacterium found in these sulfureta was Oscillatoria sp.
The depth horizon at which maximum populations of purple sulfur bacteria were recorded often did not coincide with the sulfide/oxygen interface but was located closer to the sediment surface where polysulfides, polythionates, elemental sulfur and occasionally thiosulfate were present. The structure of these sulfureta is discussed in relation to the chemolithotrophic growth capacities of Thiocapsa in the presence of oxygen.     

Physiology of sulfide in the rat colon: use of bismuth to assess colonic sulfide production.

Colonic bacteria produce hydrogen sulfide, a toxic compound postulated to play a pathogenetic role in ulcerative colitis. Colonic sulfide exposure has previously been assessed via measurements of fecal sulfide concentration. However, we found that <1% of fecal sulfide of rats was free, the remainder being bound in soluble and insoluble complexes. Thus fecal sulfide concentrations may reflect sulfide binding capacity rather than the toxic potential of feces. We utilized bismuth subnitrate to quantitate intracolonic sulfide release based on observations that bismuth 1) avidly binds sulfide; 2) quantitatively releases bound sulfide when acidified; and 3) does not influence fecal sulfide production by fecal homogenates. Rats ingesting bismuth subnitrate excreted 350 +/- 18 micromol/day of fecal sulfide compared with 9 +/- 1 micromol/day in control rats. Thus the colon normally absorbs approximately 340 micromol of sulfide daily, a quantity that would produce local and systemic injury if not efficiently detoxified by the colonic mucosa. Studies utilizing bismuth should help to clarify the factors influencing sulfide production in the human colon.     

Competition for Dimethyl Sulfide and Hydrogen Sulfide by Methylophaga sulfidovorans and Thiobacillus thioparus T5 in Continuous Cultures

Pure and mixed cultures of Methylophaga sulfidovorans and Thiobacillus thioparus T5 were grown in continuous cultures on either dimethyl sulfide, dimethyl sulfide and H(inf2)S, or H(inf2)S and methanol. In pure cultures, M. sulfidovorans showed a lower affinity for sulfide than T. thioparus T5. Mixed cultures, grown on dimethyl sulfide, showed coexistence of both species. M. sulfidovorans fully converted dimethyl sulfide to thiosulfate, which was subsequently further oxidized to sulfate by T. thioparus T5. Mixed cultures supplied with sulfide and methanol showed that nearly all the sulfide was used by T. thioparus T5, as expected on the basis of the affinities for sulfide. The sulfide in mixed cultures supplied with dimethyl sulfide and H(inf2)S, however, was used by both bacteria. This result may be explained by the fact that the H(inf2)S-oxidizing capacity of M. sulfidovorans remains fully induced by intracellular H(inf2)S originating from dimethyl sulfide metabolism.     

Modulation of sulfide oxidation and toxicity in rat mitochondria by dehydroascorbic acid

Hydrogen sulfide is enzymatically produced in mammalian tissues and functions as a gaseous transmitter. However, H(2)S is also highly toxic as it inhibits mitochondrial respiration at the level of cytochrome c oxidase, which additionally is involved in sulfide oxidation. The accumulation of toxic sulfide levels contributes to the pathology of some diseases. This paper demonstrates that sulfide toxicity can be modified, and dehydroascorbic acid functions as an effector in this process. It significantly reduces the inhibitory effect of sulfide on cytochrome c oxidase, resulting in higher rates of respiration and sulfide oxidation in rat mitochondria. After the addition of dehydroascorbic acid mitochondria maintained more than 50% of the oxygen consumption and ATP production rates with different substrates in the presence of high concentrations of sulfide that would normally lead to complete inhibition. Dehydroascorbic acid significantly increased the sulfide concentration necessary to cause half maximal inhibition of mitochondrial respiration and thus completely prevented inhibition at low, physiological sulfide concentrations. In addition, sulfide oxidation was stimulated and led to ATP production even at high concentrations. The decrease in sulfide toxicity was more pronounced when analyzing supermolecular functional units of the respiratory chain than in isolated cytochrome c oxidase activity. Furthermore, the protective effect of dehydroascorbic acid at high sulfide concentrations was completely abolished by quantitative solubilization of mitochondrial membrane proteins with dodeclymaltoside. These results suggest that binding of cytochrome c oxidase to other proteins probably within respiratory chain supercomplexes is involved in the modulation of sulfide oxidation and toxicity by dehydroascorbic acid.     

Rapid hydrogen sulfide consumption by Tetrahymena pyriformis and its implications for the origin of mitochondria

Although sulfide is typically regarded as toxic to eukaryotic cells, it is avidly consumed by Tetrahymena pyriformis. That was observed only when the sulfide concentration was kept below 1 microM. Previously concentrations that were too high had been tested. A new device (Sulfidostat) was used to measure sulfide consumption in steady-state concentrations as low as 10(-12)M. The technique was validated non-biologically by slowly injecting AgNO(3) into buffer and using Ag(2)S precipitation to mimic sulfide consumption, confirming that rates of sulfide consumption could be measured independently of sulfide concentrations. With T. pyriformis, sulfide consumption was 0.25 micromol (gprotein)(-1)s(-1) in 0.5 microM sulfide. Sulfide consumption required O(2) and was inhibited by HCN or by too much sulfide. When cells were separated into fractions, sulfide consumption occurred in the particulate (mitochondrial) fraction. Unexpectedly, the soluble cytosolic fraction slowly produced sulfide even when aerated. The observations are consistent with the conjecture that mitochondria evolved from sulfidotrophic symbionts in a sulfidogenic host cell.     

Hydrogen sulfide consumption measured at low steady state concentrations using a sulfidostat

Although >10 microM hydrogen sulfide typically is toxic to eukaryotic cells, <1 microM sulfide is rapidly consumed and oxidized. To measure sulfide consumption in such low concentrations, we built a "Sulfidostat." The apparatus uses a sulfide-specific electrode to measure the concentration of free sulfide. The electrode is connected to a computer that controls a syringe pump. The pump injects Na(2)S solution into the sample chamber to maintain a constant concentration. Since the response of the electrode to low sulfide concentrations at neutral pH had not been previously validated, that was measured. Then using the Sulfidostat, the rate of sulfide consumption is the rate at which it is pumped into the sample to maintain a constant concentration. The protozoan Tetrahymena pyriformis was used to demonstrate the apparatus; maximum sulfide consumption occurred near 0.5 microM sulfide at a rate of 250 nmol (g protein)(-1) s(-1). That is higher than the rate calculated from the disappearance of sulfide following a bolus addition, a difference that can be explained by the slow response of the electrode and by reversible binding of sulfide by the cells. The Sulfidostat can measure sulfide consumption at concentrations lower than previously have been possible.     

Kinetic parameters of a mixed culture oxidizing sulfide and sulfur with oxygen

Kinetic parameters of biological sulfide oxidation are described. The influence of the sulfide loading rate on growth yield and specific oxidation rate were investigated with free-cell suspensions. It is concluded that at least two types of bacteria were present, namely, sulfate producers (type A) that grow at higher loading rates. Type A bacteria have a growth yield of 04 g dry S/mol S, while type B bacteria have a growth yield of 04 g dry S/mol S. Type A has a high affinity for sulfide and is inhibited by sulfide at sulfide concentrations exceeding 10 mg/L. Type B has a low affinity for sulfide and is not inhibited by sulfide, but by oxygen.     

Coupled enzymatic production of sulfite, thiosulfate, and hydrogen sulfide from sulfur: purification and properties of a sulfur oxygenase reductase from the facultatively anaerobic archaebacterium Desulfurolobus ambivalens.

From aerobically grown cells of the extremely thermophilic, facultatively anaerobic chemolithoautotrophic archaebacterium Desulfurolobus ambivalens (DSM 3772), a soluble oxygenase reductase (SOR) was purified which was not detectable in anaerobically grown cells. In the presence of oxygen but not under a hydrogen atmosphere, the enzyme simultaneously produced sulfite, thiosulfate, and hydrogen sulfide from sulfur. Nonenzymatic control experiments showed that thiosulfate was produced mainly in a chemical reaction between sulfite and sulfur. The maximum specific activity of the purified SOR in sulfite production was 10.6 mumol/mg of protein at pH 7.4 and 85 degrees C. The ratio of sulfite to hydrogen sulfide production was 5:4 in the presence of zinc ions. The temperature range of enzyme activity was 50 to 108 degrees C, with a maximum at 85 degrees C. The molecular mass of the native SOR was 550 kilodaltons, determined by gel filtration. It consisted of identical subunits with an apparent molecular mass of 40 kilodaltons in sodium dodecyl sulfate-gel electrophoresis. The particle diameter in electron micrographs was 15 /+- 1.5 nm. The enzyme activity was inhibited by the thiol-binding reagents p-chloromercuribenzoic acid, N-ethyl maleimide, and 2-iodoacetic acid and by flavin adenine dinucleotide, Fe3+, and Fe2+. It was not affected by CN-, N3-, or reduced glutathione.     

Morphological and Ecophysiological Adaptations of the Marine Oligochaete Tubificoides benedii to Sulfidic Sediments

SYNOPSIS. The marine oligochaete worm Tubificoides benedii inhabitscoastal tidal sediments in which sulfide can reach toxic concentrations.The role of external ironsulfide deposition in sulfide detoxificationis discussed together with a review of morphological and ecophysiologicaladaptations of T. benedii to sulfide. The body wall of T. benediiturns black in the presence of sulfide. Histochemical studiesand micro-X-rayanalyses provide evidence for the reaction ofiron in the mucus layer above the cuticle of the worm with environmentalsulfide to produce ironsulfide. The deposited ironsulfides areeither reoxidized or shed off through moulting, a process otherwiseunknown in oligochaetes. However, calculations on the diffusionrate of sulfide into T. benedii show that the deposition ofironsulfides do not play an important role in sulfide detoxification.The first and last few segments of T. benedii are not blackenedby sulfide and do not appear to precipitate sulfide. The diffusionrate of sulfide through these segments is so rapid that internalsulfide concentrations reach levels inhibitory to cytochromec oxidase, the key enzyme of aerobic respiration, within minutes.When internal sulfide concentrations increase to toxic levels,reliance on an anaerobic metabolism represents a successfulmechanism of sulfide tolerance in T. benedii. Metabolic adaptationsto hypoxia and sulfide include the maintenance of aerobic pathwaysdespite low oxygen or high sulfide concentrations and the abilityto gain energy through anaerobic pathways when oxygen and/orsulfide concentrations become limiting