Biooxidation of a gold-containing sulfide concentrate in relation to changes in physical and chemical conditions

The growth of a microbial community and the oxidation of iron- and sulfur-containing substrates in batch culture during the leaching/oxidation of the flotation concentrate of refractory gold-arsenic sulfide ore were optimized with respect to the following medium parameters: temperature, pH, and requirement in organic substances. It was revealed that the optimum mode is (i) to maintain the pH at 1.6–1.7 and the temperature at 34–35 and 38°C and (ii) to add Corg in the form of yeast extract (0.02%). Mutually beneficial or competitive relationships among groups of microorganisms of the community were established, depending on the cultivation conditions.     

Biooxidation of a gold-bearing pyrite-arsenopyrite concentrate

Abstract: Two years of BIOX pilot plant data have been examined for steady state conditions and then correlated using logistic kinetics. It was found that the logistic equation not only predicted the performance of individual stages but also the degree of biooxidation across the entire cascade of bioreactors. It was found that the rate constant was 1.3 day^-1 in the first three stages and 0.3 day^-1 in the fourth stage. The maximum removal constant was 0.90 in stage 1 and 0.99 in the remaining stages. Plant retention time ranged from 4 to 12 days with corresponding sulphide oxidation varying from 82 to 98% respectively, and primary stage removal rates varying from 8.9 to 4.4 kg m^-3 day^-l, respectively. In addition, batch biooxidation data were obtained. The biooxidation rate was found to be about half that for the continuous bioreactors. This is in agreement with the findings of several other workers. The specific rates of bioxidation of pyrite and arsenopyrite were very similar for the bulk concentrate at about 0.15 day^-1. However, it was significant that the biooxidation of arsenopyrite in the mixed mineral preceded that of pyrite, suggesting a sequential mechanism. Gold liberation was found to be linearly related to arsenopyrite biooxidation but oxidation of pyrite appears to be preferential in the gold-rich regions.     

Biooxidation of gold-bearing sulfide ore and subsequent biological treatment of cyanidation residues

The percolation biooxidation parameters of ore from the Bakyrchik deposit were studied. An investigation of the technological parameters (such as the concentration of leaching agents, irrigation intensity, and pauses at various stages of the leaching) revealed the optimal mode for precious metal extraction. The stages of the ore processing were biooxidation, gold extraction by cyanidation or thiosulfate leaching, and biological destruction of cyanide. The gold and silver recovery rates by cyanidation were 64.0 and 57.3%, respectively. The gold and silver recovery rates by thiosulfate leaching were 64.0 and 57.3%, respectively. Gold and silver recovery rates from unoxidized ore (control experiment) by cyanidation were 20.9 and 26.8%, respectively. Thiosulfate leaching of unoxidized ore allowed the extraction of 38.8 and 24.2% of the gold and silver, respectively. Cyanidation residues were treated with bacteria of the genus Alcaligenes in order to destruct cyanide.     

Microbiological leaching of a zinc sulfide concentrate

The microbiological extraction of zinc from a high-grade zinc sulfide concentrate has been investigated, using a pure strain of Thiobacillus ferrooxidans. Conditions such as temperature, pH, pulp density, nutrient, concentration, and specific surface of solids have been studied in terms of their effects on zinc extraction rate and in some instances on final zinc concentration in solution. Where appropriate, optimum conditions for leaching have been specified.     

Release behavior of allyl sulfide from cyclodextrin inclusion complex of allyl sulfide under different storage conditions

The stability of allyl sulfide, an organosulfur compound present in garlic oil, in its α-, β-, and γ-cyclodextrin inclusion complexes was investigated under various storage conditions. The complexes of cyclodextrins and allyl sulfide were prepared by spray drying. The storage temperature, relative humidity, and initial moisture content of the inclusion complex had different effects on the release rate of allyl sulfide. Allyl sulfide in α-cyclodextrin complexes had a lower release rate than in β- and γ-cyclodextrin complexes at 100 °C and at 50 °C under 6, 40, 54, and 73% relative humidity. The initial moisture content affected only the release rate of allyl sulfide from α-cyclodextrin complexes. The release behavior of allyl sulfide can be correlated with the first-order release rate equation with a normal Gaussian distribution of free energy of activation of release rate constant. The results indicated α-cyclodextrin is a suitable material for controlled release of allyl sulfide.     

Bioleaching of zinc sulfide concentrate by Thiobacillus ferrooxidans

The kinetics of the bioleaching of ZnS concentrate by Thiobacillus ferrooxidans was studied in a well-mixed batch reactor. Experimental studies were made at 30 degrees C and pH 2.2 on adsorption of the bacteria to the mineral, ferric iron leaching, and bacterial leaching. The adsorption rate of the bacteria was fairly rapid in comparison with the bioleaching rate, indicating that the bacterial adsorption is at equilibrium during the leaching process. The adsorption equilibrium data were correlated by the Langmuir isotherm, which is a useful means for predicting the number of bacteria adsorbed on the mineral surface. The rate of chemical leaching varied with the concentration of ferric iron, and the first-order reaction rate constant was determined. Bioleaching in an iron-containing medium was found to take place by both direct bacterial attack on the sulfide mineral and indirect attack via ferric iron. In this case, the ferric iron was formed from the reaction product (ferrous iron) through the biological oxidation reaction. To develop rate expressions for the kinetics of bacterial growth and zinc leaching, the two bacterial actions were considered. The key parameters appearing in the rate equations, the growth yield and specific growth rate of adsorbed bacteria, were evaluated by curve fitting using the experimental data. This kinetic model allowed us to predict the liquid-phase concentrations of the leached zinc and free cells during the batch bioleaching process.     

Continuous culture of Thiobacillus ferrooxidans on a zinc sulfide concentrate

A zinc sulfide concentrate was leached microbiologically by Thiobacillus ferrooxidans in a continuous stirred tank reactor. A model was developed to predict, the leaching kinetics when the bacterial growth rate was not limited by any substrate other than the zinc concentrate, and it was modified to explain the observed results. Stable steady sates were obtained over a range of dilution rates from 0.0171 to 0.1038 hr^?1. Because a solid substrate was used, the specific growth rate of the bacaeria was not a unique function of the subastrate concentration, and conventional contnuous culture theory based on the Monod equation did not apply to this system. The leaching rates and bacterial growth rates were first order in mineral surface area cocentration.     

CO2 supply in the biooxidation of an enargite-pyrite gold concentrate

CO2 supply at 4% (v/v) in air increased the biooxidation of a gold concentrate (41% enargite, 43% pyrite) with Thiobacillus ferrooxidans in a 2-l bioreactor at 4% (w/v) solids concentration, 35°C and pH 2.4. Extraction increased from 21 to 69% for Fe, 19 to 25% for As, and 16 to 19% for Cu. Suspended biomass increased from 2.6·107 to 1.2·108 cells/ml. It is concluded that the biooxidation of this gold concentrate is limited by the rate of CO2 supply. © Rapid Science Ltd. 1998     

高硫高砷金精矿生物预氧化条件优化

摘要:【目的】研究温度以及返回液添加量对体系中氧化效果以及金(Au)氰化浸出率的影响。【方法】针对某高硫高砷金精矿建立了一套连续生物预氧化体系(氧化时间6 d),比较不同的温度(40℃和45℃)和返回液添加量(0和600mL)对生物预氧化效果的影响:间隔8 h连续测定氧化体系中的氧化液、氧化渣以及氰化渣中的总Fe、总S、总As以及SO4 2－和Au含量;并用16S rRNA基因克隆文库的方法对体系中的浸矿菌群结构进行分析。【结果】结果显示,提高温度和添加氧化返回液都会改变体系:升高温度在一定程度上提高了体系的氧化程度,主要表现为显著降低了尾渣中总铁、总硫含量,显著提高了尾渣中的S6 + 比例,并且降低前三槽氧化体系的耗碱量;投加返回液则会降低体系的氧化程度,主要表现为显著提高了尾渣金品位和铁含量,显著降低了尾渣中的S6 + 以及Au 浸出率;Dissimilarity和DCA结果表明温度变化对体系的影响更为显著;氧化过程中的Au 浸出率、硫氧化率以及As 去除率,三者互为显著正相关;克隆文库结果显示,该浸矿菌群主要包括3类细菌: Acidithiocacillus caldu (71%)、Leptospirillum ferriphilum (23%)和Sulfobacillus thermosulfidooxidans(6%),基于97%相似性的OTU覆盖率达93.67%。【结论】研究结果表明,相对于添加返回液,温度变化会更显著的改变体系反应效率。提高体系温度有利于矿物的氧化,而添加返回液会降低Au浸出率。本文首次研究了连续生物预氧化过程中温度梯度和返回液添加对体系的影响,本研究结果对中温生物预氧化工业生产的工艺优化、降低工业运行成本具有重要的指导意义。     

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.     

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.     

Biooxidation of monoterpenes with bacterial monooxygenases

Biotechnological monoterpene oxidation has a considerable economic potential as an alternative route to natural monoterpenoid compounds with desirable organoleptic and pharmaceutical properties. Bacterial cytochrome P450 monooxygenases (CYPs) constitute ideal catalysts for monoterpene oxidation due to their pronounced selectivities, comparably high activities and ease of recombinant expression. Research activities of the recent decades resulted in the identification and characterization of many monoterpene oxidizing bacterial CYPs, often together with their electron transfer partners. To the authors’ knowledge, no industrial process of bacterial monoterpene oxidation has been established up to date. However, the last decade has seen movement away from small scale test tube sized reactions to research activities focusing on more sophisticated processes in larger volumes and in bioreactors. These research activities successfully combined improvements on all levels of a biotransformation process. Activity, selectivity and stability of bacterial CYPs were enhanced by rational protein design, substrate and product toxicity was counteracted with the development of feeding strategies and in situ product removal techniques. The disadvantage of costly cofactors was bypassed by the application of cofactor regeneration systems and by electrochemical substitution of cofactors.     

木瓜籽毛油精炼条件筛选及其理化指标分析

以磷脂含量为指标对木瓜〔Chaenomeles sinensis ( Thouin) Koehne〕籽毛油水化脱胶过程中脱胶剂种类、脱胶剂添加量、脱胶时间、加水量和脱胶温度进行单因素实验,并在此基础上对脱胶时间、加水量和脱胶温度进行L9(33)正交实验;以酸价为指标对碱炼脱酸过程中的碱液(NaOH溶液)浓度、碱炼温度和超碱用量进行单因素实验和L9(33)正交实验;并比较了毛油、脱胶油、脱酸油和精炼油的主要理化指标变化。单因素实验和正交实验结果表明：在木瓜籽毛油水化脱胶过程中采用不同的脱胶剂种类(包括柠檬酸、草酸和蒸馏水)、脱胶剂添加量(质量分数0.1%~0.5%)、脱胶时间(10~70 min)、加水量(质量分数1%~6%)和脱胶温度(65℃~85℃),毛油中的磷脂含量均有明显差异;而碱炼脱酸过程中采用不同的碱液浓度(质量分数6%~14%)、碱炼温度(40℃~80℃)和超碱用量(质量分数0.15%~0.40%),毛油酸价也有明显变化。总体上看,木瓜籽毛油水化脱胶的适宜条件为添加质量分数0.2%柠檬酸为脱胶剂、脱胶温度75℃、加水量为质量分数4%、脱胶时间50 min;碱炼脱酸的适宜条件为碱液浓度为质量分数12%、碱炼温度80℃、超碱用量为质量分数0.30%。理化指标的测定结果表明：与毛油相比,脱胶油、脱酸油和精炼油的碘值略升高但差异不明显、过氧化值明显升高、磷脂含量和皂化值均明显下降,而脱酸油和精炼油的酸价也明显下降。研究结果显示：经过脱胶、脱酸、水洗干燥一系列过程后获得的木瓜籽精炼油的理化指标基本符合国家食用植物油卫生标准。     

Process simulation and gate-to-gate life cycle assessment of hydrometallurgical refractory gold concentrate processing

Purpose

Currently, almost all cyanide-free gold leaching processes are still in the development stage. Proactively investigating their environmental impacts prior to commercialization is of utmost importance. In this study, a detailed refractory gold concentrate process simulation with mass and energy balance was built for state-of-the-art technology with (i) pressure oxidation followed by cyanidation and, compared to alternative cyanide-free technology, with (ii) pressure oxidation followed by halogen leaching. Subsequently, the simulated mass balance was used as life cycle inventory data in order to evaluate the environmental impacts of the predominant cyanidation process and a cyanide-free alternative.

Methods

The environmental indicators for each scenario are based on the mass balance produced with HSC Sim steady-state simulation. The simulated mass balances were evaluated to identify the challenges in used technologies. The HSC Sim software is compatible with the GaBi LCA software, where LCI data from HSC-Sim is directly exported to. The simulation produces a consistent life cycle inventory (LCI). In GaBi LCA software, the environmental indicators of global warming potential (GWP), acidification potential (AP), terrestrial eutrophication potential (EP), and water depletion (Water) are estimated.

Results and discussion

The life cycle assessment revealed that the GWP for cyanidation was 10.1 t CO₂-e/kg Au, whereas the halogen process indicated a slightly higher GWP of 12.6 t CO₂-e/kg Au. The difference is partially explained by the fact that the footprint is calculated against produced units of Au; total recovery by the halogen leaching route for gold was only 87.3%, whereas the cyanidation route could extract as much as 98.5% of gold. The addition of a second gold recovery unit to extract gold also from the washing water in the halogen process increased gold recovery up to 98.5%, decreasing the GWP of the halogen process to 11.5 t CO₂-e/kg Au. However, both evaluated halogen processing scenarios indicated a slightly higher global warming potential when compared to the dominating cyanidation technology.

Conclusions

The estimated environmental impacts predict that the development-stage cyanide-free process still has some challenges compared to cyanidation; as in the investigated scenarios, the environmental impacts were generally higher for halogen leaching. Further process improvements, for example in the form of decreased moisture in the feed for halide leaching, and the adaptation of in situ gold recovery practices in chloride leaching may give the cyanide-free processing options a competitive edge.

     

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.     

A growth model for the continuous microbiological leaching of a zinc sulfide concentrate by Thiobacillus ferrooxidans

The leaching of a zinc sulfide concentrate by Thiobacillus ferrooxidans was investigated in continuous stirred tank reactors. A mathematical model for the growth of T. ferrooxidans on this solid substrate is presented and tested. Experimental leaching studies were done using two reactors in series with and without recycle of solids from the outlet of the first reactor back to its inlet. The proposed model fits the authors' experimental data well. However, comparison of the parameters calculated with those calculated from the data of others showed that a wide variation can exist; thus, the parameters seem to depend on the nature of the substrate. The area occupied on the sulfide surface by a bacterium was found to be 5.4 mum(2). The calculated maximum specific growth rates ranged from 0.20 to 0.31 h(-1), and these values were dependent on whether they were observed in the first or second of the two reactors in series.     

Bio-oxidation of a refractory gold bearing high arsenic sulphide concentrate: A pilot study

Abstract: A modular mobile bioleach pilot plant has been designed and constructed by Coastech Research Inc. The pilot plant was designed to be transported on two flatbed trucks to any location in North America for on-site piloting.The first bioleach demonstration pilot study was completed on a refractory gold bearing high arsenic (7.5% As) sulphide (28.9cf S) flotation concentrate. A production capacity of up to 562 kg per day at a feed solids concentration of approximately 14Of (w/w) solids and overall retention time of 115 h was achieved under steady operating conditions. Sulphide oxidation exceeded 75% while almost complete arsenic solubilization was observed for the final bioleached product. Oxygen and carbon dioxide uptake rates were obtained from off gas analyses. Oxygen uptake rates as high as 0.99 kg h^-1 m³ were observed. A critical dissolved oxygen concentration, to maintain chemical oxidation, within the range of 0.7-1.1 ppm was observed. Carbon dioxide uptake ratcs were decreased at dissolved oxygen concentrations below approximately 0.7-0.5 ppm. Gold extraction was enhanced from approximately 5% for the pretreated flotation concentrate, to in excess of 90% for the final bioleached product. A worker environment monitoring program was undertaken during the pilot plant operation. All samples taken for air-borne and urinary monitoring were below their respective time weighted average exposure limits.     

In situ degradability of seven plant protein supplements in heifers fed high concentrate diets with different forage to concentrate ratio

Four Holstein heifers (297.5 ± 27.7 kg BW) fed high concentrate diets were used in a crossover experiment in order to characterize the rumen fermentation pattern, and to estimate by the in situ method rumen degradation kinetics of alfalfa hay and seven plant protein supplements: solvent-extracted soybean meal, solvent-extracted sunflower meal, peas (Pisum sativum L.), lupin seeds (Lupinus sp.), broadbean (Vicia faba L.), horsebean (Vicia faba L. var equina) and vetch (Vicia sativa L.), in high concentrate diets with different forage to concentrate ratio. Heifers were fitted with a ruminal cannula. The experiment was performed in two 30-day periods, 15 days of diet adaptation and 15 days of sampling. At each period, heifers were offered one of two total mixed rations (12:88 versus 30:70 forage to concentrate ratio), two heifers per diet, on ad libitum basis. After the first period, heifers switched treatments. Intake of dry matter (DM), organic matter, crude protein and neutral detergent fibre (NDF), expressed as kg/day, did not differ between treatments, but DM intake, expressed as g/kg metabolic body weight (BW), was higher in the 12:88 diet. Average rumen pH was 6.0 in both diets, and the time pH was below 5.8, which is considered as a critical threshold for fibre degradation, was the same for both treatments (10.4 ± 1.6 h). Average ammonia nitrogen and volatile fatty acid (VFA) concentrations did not differ between treatments and individual VFA proportions were typical of high concentrate diets. Average effective degradability of DM (0.62 ± 0.02) and NDF (0.25 ± 0.03) of alfalfa hay were low and no differences were detected between treatments. The same extent of NDF degradation, together with the same proportions of VFA would indicate that both diets had the same fibrolytic activity. Forage to concentrate ratio did not affect rumen nitrogen degradability of any protein supplements incubated in situ. Corrected effective degradability for small particle losses of sunflower meal (0.78) was higher than legume seeds, which were not statistically different between each other and ranged from 0.63 to 0.66. Soybean meal had the lowest degradability value (0.61). These nitrogen degradation values must be considered more valid for beef cattle formulation of high concentrate diets than data obtained with forage diets.