Leaching of nonferrous metals from copper converter slag with application of acidophilic microorganisms

The leaching process of copper and zinc from copper converter slag with ferric iron in sulfuric acid solutions obtained using the association of acidophilic chemolithotrophic microorganisms was investigated. The best parameters of chemical leaching (temperature 70°C, an initial concentration of ferric iron in the leaching solution of 10.1 g/L, and a solid phase content in the pulp of 10%) were selected. Carrying out the process under these parameters resulted in the recovery of 89.4% of copper and 39.3% of zinc into the solution. The possibility of the bioregeneration of ferric iron in the solution obtained after the chemical leaching of slag by iron-oxidizing acidophilic chemolithotrophic microorganisms without inhibiting their activity was demonstrated.     

Bioregeneration of Leaching Solutions during Two-Step Processing of Copper-Zinc Concentrate

A comparative study of the oxidation of ferrous iron ions by various cultures of acidophilic chemolithotrophic microorganisms in solutions obtained after ferric leaching of copper-zinc concentrate at 80°C has been carried out. It was shown that the use of a moderately thermophilic culture for bioregeneration of leaching solutions was preferable. At the same time, the oxidation rate of Fe²⁺ ions reached 0.88 g/(L h), or 21.1 g/(L day). We propose that the activity of the moderately thermophilic culture was due to the presence of the mixotrophic bacteria Sulfobacillus spp., which used organic products of the microbial lysis for their growth. These products were formed during high-temperature ferric leaching of the copper-zinc concentrate with the biosolution.     

The effects of bioleaching conditions on the nonferrous metals content in copper-zinc concentrate

The effects of pH and ferrous iron concentration in cultural medium on the bioleaching of copper-zinc concentrate by mesophilic and moderately thermophilic acidophilic microorganisms were studied. It was revealed that the optimum pH for bioleaching in presence of 5 g/L of ferrous iron was 1.4–1.5. It was shown that bioleaching under optimal conditions led to an increase in the copper content in solid phase from 10.1 to 14% and a decrease in the zinc content from 7.4 to 1.4%. The results of the present work demonstrate that acidophilic microorganisms can be used for treatment of complex sulfide concentrates containing copper and zinc.     

Effect of sulfur, copper, and iron deficiency on the development of cyanide resistant respiration and the cytochrome composition of Pseudomonas aeruginosa

The effect of deficiency in sulfur, copper and iron in the growth medium on cyanide resistant respiration and cytochrome composition was studied in Pseudomonas aeruginosa and Candida lipolytica. It has been shown that: cyanide resistant respiration was observed at the stationary growth phase when the two microorganisms were cultivated in a complete medium; this respiration was detected already at the phase of decelerated growth in the case of copper deficiency; iron deficiency inhibited cyanide resistant respiration in the bacterium but stimulated its appearance in the yeast; sulfur deficiency inhibited the manifestation of cyanide resistant respiration in the both microorganisms; limitation of the bacterial growth with iron resulted in the accumulation of an iron complex (identical to pyoverdin in its spectral characteristics) in the cultural broth; the deficiency of sulfur, copper and iron inhibited the synthesis of all cytochromes in the bacterium; copper deficiency inhibited only the synthesis of a + a3 in the yeast; iron deficiency inhibited the synthesis of all cytochromes in the yeast; sulfur deficiency had virtually no effect on the content of cytochromes in the yeast. A possible nature of cyanide resistant oxidases in these microorganisms is discussed.     

Copper removal from an industrial waste by bioleaching

Summary Copper contained in a solid industrial waste produced in a silicone manufacturing process was leached with spent iron medium from aThiobacillus ferrooxidans culture. Most effective leaching was observed in a continuously fed, dual reactor system. Spent iron medium was generated by growingT. ferrooxidans in 0.9 K iron medium at pH 1.5 in the first reactor, and was transferred to a second reactor in which it leached the copper from the waste. Leaching was effective at a pulp density of the waste material as high as 20%. In experiments run at a pulp density of 2.5%, the spent iron medium was most efficient in leaching copper when it was first diluted 100-fold with a mineral salts solution at pH 1.5. Removal of the copper from the waste appeared to involve its displacement by acid, dissolved mineral salts, and ferric iron. Potentials for practical application of this process are discussed.     

THE EFFECT OF THE H ION CONCENTRATION ON THE AVAILABILITY OF IRON FOR CHLORELLA SP

The data obtained in these experiments indicate clearly that unless the necessary precautions are taken to keep the iron of the culture medium in solution the results obtained by varying the H ion concentration will not represent the true effect of this factor on growth. The availability of iron in nutrient solutions has been the subject of numerous recent investigations and it is now known that iron is precipitated at the lower hydrogen ion concentrations, that the iron of certain iron salts is less likely to be precipitated than that of others, and that certain salts of organic acids tend to keep the iron in solution. In general, ferric citrate seems to be the most favorable source of iron. In addition to chemical precipitation, however, it is also possible for the iron to be removed by adsorption on an amorphous precipitate such as calcium phosphate. As this precipitate is frequently formed when nutrient solutions are made alkaline, this may account for the discordant results reported in the literature as to the availability of certain forms of iron. By omitting calcium from the culture solution iron can be maintained in a form available for growth in alkaline solutions by the addition of sodium citrate. In such solutions the maximum growth of Chlorella occurred at pH 7.5. The alkaline limit for growth has not been established as yet. In investigating the availability of iron at varying concentrations of the hydrogen ion, changes in the pH value of the solution during the course of an experiment should also be taken into account. This is especially important in unbuffered solutions. The differential absorption of the ions of ammonium salts may cause a marked increase in the hydrogen ion concentration, which in turn will cause an increase in the solubility of iron. In strongly buffered solutions as used in these experiments this effect is slight.     

A mathematical model for the bacterial oxidation of a sulfide ore concentrate

The effect of dilution rate and feed solids concentration on the bacterial leaching of a pyrite/arsenopyrite ore concentrate was studied. A mathematical model was developed for the process based on the steady-state data collected over the range of dilution rates (20 to 110 h) and feed solids concentrations (6 to 18% w/v) studied. A modified Monod model with inhibition by arsenic was used to model bacterial ferrous ion oxidation rates. The model assumes that (i) pyrite and arsenopyrite leaching occurs solely by the action of ferric iron produced from the bacterial oxidation of ferrous iron and (ii) bacterial growth rates are proportional to ferrous ion oxidation rate. The equilibrium among the various ionic species present in the leach solution that are likely to have a significant effect on the bioleach process were included in the model. (c) 1994 John Wiley & Sons, Inc.     

Reduced Sulfur in Ashes and Slags from the Gasification of Coals: Availability for Chemical and Microbial Oxidation

This study was initiated to determine if reduced sulfur contained in coal gasifier ash and slag was available for microbial and chemical oxidation because eventual large-quantity landfill disposal of these solid wastes is expected. Continuous application of distilled water to a column containing a high-sulfur-content (4% [wt/wt]) gasifier slag yielded leachates with high sulfate levels (1,300 mg of sulfate liter⁻¹) and low pH values (4.2). At the end of the experiment, a three-tube most-probable-number analysis indicated that the waste contained 1.3 × 10⁷ thiosulfate-oxidizing bacteria per g. Slag samples obtained aseptically from the column produced sulfate under both abiotic and biotic conditions when incubated in a mineral nutrient solution. Both microbial and chemical sulfate syntheses were greatly stimulated by the addition of thiosulfate to the slag-mineral nutrient solution. These results led to a test of microbial versus chemical sulfur oxidation in ashes and slags from five gasification processes. Sulfate production was measured in sterile (autoclaved) and nonsterile suspensions of the solid wastes in a mineral nutrient solution. These ashes and slags varied in sulfur content from 0.3 to 4.0% (wt/wt). Four of these wastes demonstrated both chemical (2.0 to 27 μg of sulfate g⁻¹ day⁻¹) and microbial (3.1 to 114 μg of sulfate g⁻¹ day⁻¹) sulfur oxidation. Obvious relationships between sulfur oxidation rate and either sulfur content or particle size distribution of the wastes were not immediately evident. We conclude that the sulfur contained in all but one waste is available for oxidation to sulfuric acid and that microorganisms play a partial role in this process.     

Bioregeneration of activated carbon: A review

Bioregeneration is defined as the renewal of the adsorptive capacity of activated carbon by microorganisms for further adsorption. Bioregeneration of activated carbon increases the service-life of activated carbons. It is traditionally believed that bioregeneration occurs as a result of a concentration gradient between the carbon and the bulk liquid. Therefore, bioregeneration can only occur for compounds that readily desorb. Some researchers suggest that also exo-enzymes act in bioregeneration. Bioregeneration has been demontrated in offline systems, which involve desorption and biological removal of adsorbed organic matter in a closed-loop recirculating batch system. It has also been shown that bioregeneration of carbon occurs during the time course of wastewater treatment processes that are based on biological activated carbons (BACs). However, most of the studies aiming at quantifying bioregeneration were performed using offline systems because of difficulties encountered in quantifying bioregeneration during BAC treatments of wastewater. Bioregeneration is dependent on several factors including biodegradability, adsorbability and desorbability of sorbate, characteristics of activated carbon and process configuration, and it can be optimized by varying the operational conditions. In this review, we are addressing the enhancement of biological treatment by activated carbon, the definition and mechanisms of biological regeneration, the relationship between adsorption reversibility and bioregeneration, the factors affecting bioregeneration, the methods for determination and quantification of bioregeneration and the mathematical models of bioregeneration. Future research is still required to determine the optimum conditions for an increased bioregeneration. Particularly, factors such as the activated carbon type, nature of the microbial community and optimum process configuration need further investigation. The validity and efficiency of exo-enzymatic activities on bioregeneration should still be investigated.     

Studies in the nutrition of the forage legumes

Summary The effect has been studied of varying levels of copper supply on the copper, iron and manganese contents of plants ofT. subterraneum in which the growth rate had been altered by variation in nitrate supply and light intensity.It has been found that the copper content of the plants is related logarithmically to the level of copper in the nutrient and is not affected by nitrate supply or intensity of illumination. Within the limits set, there is no change in the copper content of the tops with time, but the concentration in the roots shows a progressive increase, particularly at the higher levels of copper supply. Between one-fifth and one-quarter of the copper present in the roots is in the free space.The concentration of both iron and manganese decline with increase in copper supply. Although this is largely an indirect result arising from increased growth at the higher copper supply, a considerable distortion of the Fe/Mn ratio can occur. In the roots, however, there appears to be a direct restrictive effect of the higher copper supply on manganese concentration, over and above the indirect effect of growth dilution.The data on which this paper is based are mainly from the these submitted by M. G. Yates, P. E. Cansfield and J. T. Saul for the degree of Ph.D. of the University of Nottingham.     

Dephosphorization of LD slag by phosphorus solubilising bacteria

Phosphorus is one of the major nutrients, and microbial solubilisation of insoluble mineral phosphate in soil is an important process in natural ecosystem and in agricultural soil. Many soil microorganisms display the ability to solubilize many insoluble inorganic phosphates. They are generally referred as phosphorus solubilising microorganisms (PSM). In this study an attempt was made to look into the phosphorus solubilisation efficiency of some commonly available soil bacteria and their possible application in bio-beneficiation of metallurgical waste like LD Slag. Linz -Donawitz (LD) slag is produced in large quantities (200 kg LD slag per ton of hot metal) and poses a substantial disposal problem in the iron and steel making industry. LD slag contains around 29% Ca, 21% Fe, and 5% Mg. Its phosphorus content is about 1.5-6%. Due to presence of high amount of Ca, it can be used as flux in blast furnace, but presence of high amount of phosphorus in the LD slag makes them unsuitable for industrial application. Removal of phosphorus with the help of phosphorus solubilising microorganisms may be a great advantage in biotechnological applications. Two gram positive bacteria belonging to genus Bacillus and two gram negative bacteria belonging to genus Pseudomonas were selected in this study. Phosphorus solubilisation efficiency was studied initially with tricalcium phosphate as model insoluble phosphate compound at different sugar concentration, NaCl concentration and at different initial pH of the medium. About 35% of ‘P’ could be solubilized from LD slag by Pseudomonas aeruginosa at 2% solid content.     

The effects of Fe(II) and Fe(III) concentration and initial pH on microbial leaching of low-grade sphalerite ore in a column reactor

In this study the effects of initial concentration of Fe(II) and Fe(III) ions as well as initial pH on the bioleaching of a low-grade sphalerite ore in a leaching column over a period of 120 days with and without bacteria were investigated. Four different modifications of medium were used as column feed solutions to investigate the effects of initial concentration of Fe(II) and Fe(III) ions on zinc extraction. The experiments were carried out using a bench-scale, column leaching reactor, which was inoculated with mesophilic iron oxidizing bacteria, Acidithiobacillus ferrooxidans, initially isolated from the Sarcheshmeh chalcopyrite concentrate (Kerman, Iran). The effluent solutions were periodically analyzed for Zn, total Fe, Fe(II) and Fe(III) concentrations as well as pH values. Bacterial population was measured in the solution (free cells). Maximum zinc recovery in the column was achieved about 76% using medium free of initial ferrous ion and 11.4 g/L of ferric ion (medium 2) at pH 1.5. The extent of leaching of sphalerite ore with bacteria was significantly higher than that without bacteria (control) in the presence of ferrous ions. Fe(III) had a strong influence in zinc extraction, and did not adversely affect the growth of the bacteria population.     

Thermophilic vs. mesophilic bioleaching process performance

Abstract: Mesophilic and thermophilic mineral oxidising microbial cultures were compared for their capacity to leach both a complex pyritic and an arsenopyritic ore, aiming at copper and gold recovery, respectively. The mesophilic cultures are primarily based on the activity of Thiobacillus -type microorganisms, while the thermophile characteristics place them in the sulphur metabolizers branch df Archaebacteria. Study of key process variables and determination of their optimum values were carried out to provide a basis for significant physiological and technical comparison. Each microbial culture finds a preferential process application, depending on the choice of the reactor and ore.     

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.     

Redistribution of metal ions to control low density lipoprotein oxidation in Ham's F10 medium

The study of cell-mediated low density lipoprotein (LDL) oxidation has traditionally been undertaken using Ham's F10 media due to its high metal content and low levels of antioxidants. Although there has been no acknowledged change to this media in recent years by the suppliers, Ham's F10 medium has been found to be extremely inconsistent in its promotion of LDL oxidation in the absence of cells. This variability contrasts with the relatively consistent rates of THP-1 cell-mediated LDL oxidation. This study has now shown that the variability in cell-free LDL oxidation is medium-dependent and not an artefact of experimental protocol. It presents evidence that suggests the variable rates of cell-free LDL oxidation are caused by iron auto-oxidation during storage of the Ham's F10 medium. The medium can be standardized by removal of all transition metals, by treatment with Chelex, before the addition of known amounts of iron or copper. This treatment generates a cell culture medium that only allows very slow LDL oxidation in the absence of cells.     

Migration of arsenic(III) during bacterial oxidation of arsenopyrite in chalcopyrite concentrate by Thiobacillus ferrooxidans

During bacterial oxidation of the arsenopyrite that contaminated a chalcopyrite concentrate, the bioextraction of arsenic from the concentrate was examined. A long-term constant As(III) concentration, representing a large portion of the total arsenic, occurred in the leaching medium. As(III) was not further oxidized, either under bioextraction conditions or by Fe(III) in the presence of the mesophilic bacterium Thiobacillus ferooxidans. These results are discussed in relation to the influence of leaching microorganisms on the form of arsenic in the solution. Dissolved As(III) could be reversed into a solid phase by adsorption of As(III) by forming an iron precipitate. Correspondence to: M. Mandl     

Nutritional Requirements of the Micro-organisms Active in the Oxidation of Ferrous Iron in Acid Mine Leach Liquors

The nutritional requirements for the oxidation of ferrous iron in acid mine water by fixed films of micro-organisms were investigated. Supplementing the mine leach liquor with additional ammonium, phosphate and potassium did not improve the efficiency of ferrous iron oxidation. The minimum non-limiting requirement of the ferrous iron oxidizing organisms for these nutrients was (mg/l): ammonium, 10; phosphate, 45, and potassium, 2·5. A strain of Thiobacillus was isolated which was able to grow on a medium to which only dihydrogen potassium phosphate, ferrous sulphate and agar had been added.     

A two-stage technology for bacterial and chemical leaching of copper-zinc raw materials by Fe<Superscript>3+</Superscript> ions with their subsequent regeneration by chemolithotrophic bacteria

A two-stage technology for bacterial and chemical leaching of nonferrous metals in a specifically designed laboratory unit has been proposed. At the first stage of leaching, ferric iron formed during the second stage of oxidation of Fe²⁺ ions by mesophilic chemolithotrophic microorganisms was used. The optimal parameters of the first stage of the process (flow rate, temperature, and the process duration) were 2 l/h, 75°C, and 24 h, respectively. The results of testing of the two-stage technology for leaching copper-zinc raw materials indicated that the depth of zinc and copper leaching can be increased from 70 to 93% and from 40 to 58.8%, respectively, and the process duration can be reduced from 120 to 24 h as compared to the commonly used one-stage technology.     

Lolium multiflorum uptake of iron supplied as different synthetic chelates

The plant availability of Fe from synthetic chelates has not been examined extensively for plants having the second strategy in iron uptake. Since these plants also excrete chelating agents, competition between natural and synthetic ligands is expected. This research was conducted to study the efficiency of different iron-chelates (Fe-EDTA, Fe-DTPA, Fe-EDDHA and a commercial product, Rexene) inLolium multiflorum iron nutrition. Plants were grown in a greenhouse with hydroponic culture using a buffered nutrient solution at pH 8. Initial iron concentration in the nutrient solution was near 0.5 mgl^–1 and solutions were replaced weekly. In an other Fe-EDTA treatment the same amount of chelate was supplied by four additions during each week.Changes of iron concentration in the nutrient solution, harvestable yield, Fe, Mn, Cu and Zn content in plant tissue and chlorophylllevels in leaves are discussed as parameters to evaluate chelate efficacy. Fe-EDDHA, without inorganic iron in the medium was not as effective as the commercial product Rexene, containing Fe-EDDHA and some extra weakly complex iron, which gave the highest yields. Fe-EDTA applied once a week with fresh nutrient solution was less effective than a four part addition as seen from Chl₁/[Fe] ratios.     

Effect of Water Potential on Growth and Iron Oxidation by Thiobacillus ferrooxidans

The effect of water potential on the growth of two strains of Thiobacillus ferroxidans was determined by adding defined amounts of sodium chloride or glycerol to the culture medium. The two strains differed slightly, and the most tolerant strain had a minimum water potential for growth of -15 to -32 bars when sodium chloride was used and -6 bars when glycerol was used. In another approach, the limiting water potential was determined by equilibrating small amounts of culture medium with atmospheres of relative humidities equivalent to specific water potentials, and the ability of the organism to grow and oxidize ferrous iron was determined. Under these conditions, which are analogous to those which might control water potential in a coal refuse pile or copper leaching dump, the lower limit at which iron oxidation occurred was -23 bars. The water potential of some coal refuse materials in which T. ferrooxidans was present were determined, and it was found that the water potentials at which the organism was active in these habitats were similar to those at which it was able to grow in culture. However, marked variation in water potential of coal refuse materials was found, presumably due to differences in clays and organic materials, and some coal refuse materials would probably never have water potentials at which the organism could grow. Some literature on the water potentials in copper leach dumps is reviewed, and it is concluded that control of water potential is essential to maximize the success of leaching operations. Because adequate drainage is necessary in a leach dump to ensure sufficient aeration, in many cases water availability in leach dumps may restrict the development of the bacterium necessary for the process.