Trans. Nonferrous Met. Soc. China 25(2015) 3103-3110

Bioleaching and electrochemical property of marmatite by Sulfobacillus thermosulfidooxidans

Xian-xue XIONG, Guo-hua GU, Jin-rong BAN, Shuang-ke LI

School of Minerals Processing and Bioengineering, Central South University, Changsha 410083, China

Received 13 October 2014; accepted 10 January 2015

Abstract:

Bioleaching and electrochemical experiments were conducted to evaluate marmatite dissolution in the presence of pure S. thermosulfidooxidans. The effects of particle size, pH controlling and external addition of Fe³⁺ ions on the zinc extraction were investigated. The results show that in the bioleaching process the best particle size range is 0.043-0.074 mm and adjusting pH regularly to the initial value has a profound effect on obtaining high leaching rate. External addition of Fe³⁺ ions could accelerate the bioleaching, while the concentration of additional Fe³⁺ over 2.5 g/L weakens the positive effect, and even hinders the dissolution of marmatite. SEM and XRD analyses of the leaching residues reveal that a product layer composed of elemental sulfur and jarosite is formed on the mineral surface, which results in a low leaching speed at later phase. The results of electrochemical measurements illustrate that additional Fe³⁺ ions could increase the corrosion current density, which is favorable to zinc extraction. The EIS spectra show that rate-limiting step does not change when Fe³⁺ ions are added.

Key words:

marmatite; S. thermosulfidooxidans; bioleaching; jarosite; electrochemical property;

1 Introduction

Nowadays, it is widely accepted that certain microorganisms play a major role in the leaching of base and precious metals from various mineral resources [1-4]. The bioleaching of zinc sulphide using acidophilic autotrophic microorganisms has been studied extensively by some researchers in shake flasks and in columns [2,5-9], though the leaching effects reported are different in each study due to different leaching conditions and distinct properties of the mineral specimens used in the various experiments. However, there is neither total agreement on the mechanism of zinc sulphide bioleaching nor a unanimously accepted theory that explains the bioleaching process.

Marmatite is an important resource of zinc ore in China, which is difficult to be processed effectively by traditional technologies due to its high content of iron. But it is more suitable for bioleaching and the rate of oxidative dissolution is higher compared with sphalerite [10]. As moderately thermophilic micro- organisms have received increasing attention since their optimal growth temperature presents a kinetic advantage over mesophilic microorganisms. Recently, WANG et al [11] and SHI and FANG [12] investigated the bioleaching of marmatite using a moderately thermoacidophilic iron-oxidizing bacterial strain (MLY). SHI and FANG [12] demonstrated the technological feasibility of a microbiological process using MLY for extracting zinc from marmatite concentrate. And under the leaching conditions of the initial pH value 1.5, temperature 50 °C, pulp density 5%, particle size less than 35.5 μm (over 90%), over 95% of zinc dissolution was obtained [12]. WANG et al [11] discovered that, comparing with A. ferrooxidans, the supplementary addition of Fe²⁺ as a source of Fe³⁺ to be generated by bacteria was not necessary because the higher temperature improved the dissolution of marmatite in sulphuric acid, and thus acidic leaching happened before ferric ion leaching. Sulfobacillus thermosulfidooxidans is a moderately thermoacidophilic bacterium. Its optimum growth temperature is 50-53 °C and the effective growth temperature can be up to 58 °C. Sulfobacillus thermosulfidooxidans can take ferrous iron and sulphide ores as energy substances to grow autotrophically. Also, it can utilize yeast extraction to grow heterotrophically. It can be able to oxidize ferrous iron and elemental sulfur in the presence of yeast extract. Some investigations of sulphide mineral leaching were carried out by using Sulfobacillus thermosulfidooxidans. XIA et al [13] investigated the surface sulfur speciation of chalcopyrite leached by Sulfobacillus thermosulfidooxidans. Sulfobacillus thermosulfidooxidans was used to study the effect of temperature on nickel sulfide bioleaching by CRUZ et al [14], compared with mesophile (Acidithiobacillus ferrooxidans) strains, the dissolution was higher, and meanwhile the external ferrous iron adversely affected the nickel leaching at higher temperatures.

In order to discover the effect of Sulfobacillus thermosulfidooxidans on the dissolution of natural marmatite and further understand the mechanisms of marmatite bioleaching, the effects of some factors, such as particle size, pH controlling and the external addition of different concentrations of Fe³⁺ ions, on the marmatite dissolution by bioleaching experiments were studied. The mineral composition and the morphological features of the residue samples were analyzed by XRD and SEM. The mechanism of marmatite bioleaching was also studied by Tafel and electrochemical impedance spectroscopy.

2 Experimental

2.1 Marmatite preparation and mineral characters

The bioleaching tests were performed using pure marmatite (approximately above 96%). The natural marmatite ores were obtained from a lead-zinc mine in Dachang, Guangxi Province, China. The ores were splintered into small fragments with a geological hammer and selected carefully by hand. After hand- selected, the obtained samples were dry-ground by a porcelain ball milling and then sieved into different fractions.

The samples of marmatite used in the bioleaching tests were from Dachang Mine in Guangxi Province of China. The samples were splintered into small fragments with a geological hammer and dry-ground in a porcelain ball milling. Then, the products were sieved into different fractions for bioleaching experiments. The chemical composition of different fractions is listed in Table 1. X-ray diffraction (XRD) analysis in Fig. 1 shows that marmatite is the major mineral component and there is also a little amount of quartz in it.

2.2 Microorganisms and culture media

A moderately thermoacidophilic bacterium of Sulfobacillus thermosulfidooxidans, which was grown in medium using rotary shakers at 160 r/min with the initial pH of 1.6 and temperature of 53 °C and used in all experiments, was obtained from the Key Laboratory of Biometallurgy in Central South University, China. A sterilized iron-free 9K medium was used as a substrate for bacterial growth. The iron-free 9K medium consisted of (NH₄)₂SO₄ 3.0 g/L, KCl 0.1 g/L, K₂HPO₄ 0.5 g/L, MgSO₄·7H₂O 0.5 g/L and Ca(NO₃)₂ 0.01 g/L. The bacteria were routinely sub-cultured using 20 g/L ferrous sulphate and 0.02% yeast extraction as energy source in an incubator. Then, the solution was filtered through a Whatman filter No. 1 to remove the precipitate and centrifuged at 9000 r/min for 20 min using a centrifuge, Model TGL16M. The centrifuged cells were washed by sterilized sulphuric acid at pH 1.6. Washing and centrifugation were repeated three times before the cells were free from the precipitates. After that, the cells were re-suspended in the sterilized iron-free 9K medium with a concentration of 2×10⁸ cell/mL.

Table 1 Chemical composition of different fractions

Fig. 1 XRD pattern of mineral sample

2.3 Bioleaching experiments

Bioleaching experiments were carried out in 250 mL Erlenmeyer flasks. The iron-free 9K salt medium (135 mL) adjusted to the required pH was transferred into each flask. The flasks were then autoclaved at 1×10⁵ Pa and 121 °C for 20 min. Following autoclaving, each flask was inoculated with 15 mL bacterial suspension, producing a final volume of slurry of approximately 150 mL. In all experiments, the initial bacterial population was 2×10⁷ cell/mL. The flasks were shaken in rotary shakers for 30 d with a constant speed of 160 r/min and temperature of 53 °C. Ferric irons used in the experiments were added properly by analytical reagents of ferric sulfate.

During the bioleaching process, if the pH changed, it was adjusted to pH 1.6±0.03 with diluted sulfuric acid or 2 mol/L sodium hydroxide. 4 mL liquid sample was removed periodically from the flasks, and then used for the analysis of dissolved zinc content by atomic absorption spectrophotometry (AAS). The removed solutions were replaced with an equal volume of sterilized iron-free nutrient medium. The redox potentials were measured using a platinum electrode with reference to a saturated calomel electrode. The bioleaching residues were examined using X-ray diffraction (XRD) and scanning electron microscopy (SEM).

2.4 Electrochemical study

Electrochemical studies were conducted using a conventional three-electrode system electrochemical cell. The cell consists of a Ag, AgCl/KCl(saturated)-reference electrode with a salt bridge (capillary), two graphite counter electrodes, and a particularly made working electrode by the method in Refs. [12-14]. 1 g base conductor material (powdered graphite) was mixed with 1 g powdered marmatite sample and 0.5 mL paraffin oil. They were compressed under pressure using a carbon paste electrode holder.

The Tafel curves were tested with a sweep rate of 1 mV/s and applied potentials of ±250 mV vs open circuit potential (OCP). The electrochemical impedance spectroscopy studies were carried out by applying a 5 mV amplitude sine-wave signal perturbation in the frequency range of 10^-2-10^-5 Hz under the open circuit potential and the impedance diagrams were shown in the form of Nyquist plots. Before all the measurements, the pH of the electrolyte was adjusted to 1.6. There was no further adjustment when Fe³⁺ ions were added into the electrolyte.

3 Results and discussion

3.1 Bioleaching of marmatite

3.1.1 Effect of particle size

The effect of particle size on the marmatite bioleaching was studied at a rotating speed of 160 r/min. It can be seen from Fig. 2(a) that the zinc dissolution increased with decreasing particle size to a certain size (0.043-0.074 mm), below which a reverse trend was noted. A similar situation was observed by OLUBAMBI et al [15], where particles less than 75 μm did not improve the bioleaching rates, but resulted in lower recoveries. This could be explained from the view point of the surface area of the mineral, which was available for microbial attack. By decreasing the particle size, the surface area per unit mass of the mineral increased, and therefore, improved mass transfer and enhanced bioleaching rates are achieved [16]. Lower dissolution rate at particle size fraction of 0.074-0.150 mm could be attributed to the negative influence of larger particle size. Lower surface area at the larger particle size fraction could result in a decrease in the number of active microbial attachment sites and a decrease in cell viability [17]. Lower recovery at finer particle size fractions might be attributed to possible cell damage and deactivation [18], which could be caused by finer particles arising from probable oxygen deficiency due to limiting air flow rate. At the same time, reduction of particle size below a critical level could increase the extent of the particle-particle collision and impose severe attrition which might disrupt the structure of the cells [15,16]. In a word, the larger particles and finer particles both had impeding effects on microbial-mineral activities and the growth of S. thermosulfidooxidans, which could be proved by Figs. 2(b) and (c). Therefore, the particle size fraction of 0.043-0.074 should be chosen as the optimum size for bioleaching experiments.

Fig. 2 Effect of particle size on zinc extraction by S. thermosulfidooxidans

3.1.2 Effect of controlling pH

There usually was an optimal pH for the bacteria to keep them the best activity. But the pH changed during the leaching process due to the complex redox reactions in the system. In this work, the effect of controlling pH to the initial value of 1.6 at regular intervals on the dissolution of marmatite was examined. The experimental results are shown in Fig.3. It indicates that the zinc dissolution was higher when pH was adjusted to the initial value of 1.6 during the experiment process (Fig. 3(a)). This suggested that adjusting pH could promote the marmatite bioleaching by S. thermosulfidooxidans. The low zinc extraction could be credited to the higher pH values (Fig. 3(c)) without controlling pH, which might make it difficult for the thriving of S. thermosulfidooxidans and the generation of ferric ions according to the Reaction (1). At the same time, higher pH values during the leaching process without controlling pH might accelerate the formation of jarosite (Reaction (2)). It can be seen from Figs. 3(b) and (d) redox potential and concentration of iron ions were both higher under the condition of controlling pH. The results were consistent with the tendency of the dissolution rate change of marmatite.

      (1)

         (2)

3.1.3 Effect of external addition of Fe³⁺ ions

The effects of external addition of Fe³⁺ ions on the marmatite bioleaching are shown in Fig. 4. It can be seen that the addition of Fe³⁺ ions accelerated the marmatite dissolution at the beginning of the leaching experiments, since the marmatite oxidation occurred by a chemical mechanism according to Reaction (3) and the rate of bacterial oxidation of ferrous ion was low in the initial stage of experiments [7,8]. In the first 3 d, the zinc extraction rate obtained in the experiments with 2.5 g/L Fe³⁺ was 17.8%, which was almost five times that achieved in the experiments without Fe³⁺ (3.0% zinc dissolution). When the supplementary addition of Fe³⁺ was up to 7.5 g/L, the promoting effect on zinc dissolution became weaker, but the leaching rate was still higher than that without additional Fe³⁺ ions. Whereas the inhibited effect was observed when additional concentration of Fe³⁺ was up to 15 g/L. This was because high Fe³⁺ concentrations might affect the activity of bacteria [19]. Another reason for the low zinc dissolution with high Fe³⁺ concentration might be attributed to the formation of precipitation (such as jarosite) according to Reaction (2), which occurred much more easily and earlier under the condition of high Fe³⁺ concentrations. The results indicated that the chemical oxidation of Fe³⁺ ions played an important role in the zinc extraction during the leaching process, especially in the initial stage when the cell density and bacterial oxidation ability of ferrous irons were low. While it was also suggested that too high concentration of additional Fe³⁺ ions in the leaching system could inhibit the zinc extraction.

 (3)

3.1.4 SEM and XRD analyses of leaching residues

The SEM analysis results of bioleaching residues in different leaching solutions are shown in Fig. 5. It can be seen that the surfaces of the residue particles were wrapped by a reaction product layer, which inhibited the flow of microorganisms, nutrients and reaction products from mineral surface [4,10]. The layer on the residue obtained from the bioleaching with 2.5 g/L external additional Fe³⁺ ions was less porous than that without additional Fe³⁺ ions.

Fig. 3 Effect of controlling pH on zinc extraction by S. thermosulfidooxidans (3% (w/v) pulp density, 10% inoculums addition in volume fraction, and rotating speed 160 r/min)

Fig. 4 Effect of external addition of Fe³⁺ ions on zinc extraction by S. thermosulfidooxidans

Fig. 5 SEM images of leaching residues

The components of leaching residues were analyzed further by X-ray diffraction (Fig. 6). In Fig. 6, the X-ray diffraction patterns of residues leached by original S. thermosulfidooxidans after 30 d show that jarosite and sulfur formed during the leaching process. The lower leaching rate might have a relation with the passivation layer formed on the particle surface, which could hinder the bioleaching of marmatite. It can also be seen that with additional 2.5 g/L Fe³⁺ ions the intensity of peaks corresponding to jarosite was stronger than that without additional Fe³⁺ ions. This suggested that there were more jarosites produced on the surface of particle and then inhibited the dissolution of marmatite.

3.2 Electrochemical analysis

The Tafel polarization curves of the marmatite- carbon paste electrode with various concentrations of Fe³⁺ ions are described in Fig. 7. From the Tafel polarization curves, the electrochemical corrosion kinetic parameters can be obtained, which are listed in Table 2. It can be seen that the corrosion potential (φ_corr) had a significant increase with the addition of Fe³⁺ ions. The result was consistent with the tendency of open circuit potential (OCP) change. The open circuit potentials were 347, 567 and 612 mV for the Fe³⁺ concentrations of 0, 1.25 and 2.5 g/L, respectively. The J_corr in the electrolyte with Fe³⁺ ions was much higher than that without additional Fe³⁺ ions. The higher corrosion current density suggested that the dissolution rate of marmatite was higher during the experiments. In other words, the external addition of Fe³⁺ ions facilitated the extraction of marmatite [20,21]. Under the condition of 2.5 g/L additional Fe³⁺ ions the corrosion current density was 41.00 μA/cm² and declined slightly when compared with that under the condition of 1.25 g/L additional Fe³⁺ ions. This is because the higher the concentration of additional Fe³⁺ ions was, the earlier the passivation phenomenon appeared during the leaching process (Fig. 7).

Fig. 6 XRD patterns of leaching residues

Fig. 7 Effects of Fe³⁺ ions on Tafel curves of marmatite-carbon paste electrode in the presence of pure original strain of S. thermosulfidooxidans at 53 °C and scan rate of 1 mV/s with sweep range of ±250 mV (vs OCP)

Figure 8 illustrates the electrochemical impedance spectroscopy (EIS) of the marmatite-carbon paste electrode with different concentrations of additional Fe³⁺ ions under the open circuit potential. From Fig. 8, it can be seen a large capacitance loop in the tested frequency scope when the EIS measurement was carried out in the electrolyte without additional Fe³⁺ ions in the presence of S. thermosulfidooxidans, which suggested that the oxidation reaction of the marmatite was controlled by the charge transfer [21-24]. Compared with Fig. 8(a), Fig. 8(b) shows an obvious change in the EIS spectra in the system with additional Fe³⁺ ions. The loops were dramatically depressed with the addition of Fe³⁺ ions, which implied the improving function of Fe³⁺ ions on the dissolution of marmatite. But the shapes of electrochemical impedance spectroscopy were similar. These results illustrated that the rate-limiting step was not changed.

Table 2 Tafel parameters of marmatite-carbon paste electrode with different concentrations of Fe³⁺ ions in acid solution with S. thermosulfidooxidans

Fig. 8 Electrochemical impedance spectroscopy (EIS) of marmatite-carbon paste electrode in the presence of S. thermosulfidooxidans at 53 °C with different concentrations of additional Fe³⁺ ions under open circuit potential

4 Conclusions

1) Controlling pH had a positive effect on marmatite leaching by S. thermosulfidooxidans and the best particle size for bioleaching experiments was 0.043-0.074 mm. External addition of Fe³⁺ could promote zinc extraction, while the positive effect might decline when the concentration of additional Fe³⁺ ions was too high. Fe³⁺ ions played an important role in the dissolution of marmatite, especially in the initial stage when the cell density and bacterial oxidation ability of ferrous irons were low.

2) The SEM and XRD analyses showed that there was a layer wrapping on the surface of residues, which was composed of sulfur and jarosite formed in the process of bioleaching by S. thermosulfidooxidans. With additional 2.5 g/L Fe³⁺ ions more jarosites were produced than that without additional Fe³⁺ ions.

3) The electrochemical behaviors of the marmatite- carbon paste electrode showed that external addition of Fe³⁺ ions increased the corrosion current density, which meant that the dissolution of marmatite became rapid, accordingly promoted the dissolution of marmatite. The EIS spectra indicated that the rate limiting step was not changed when Fe³⁺ ions were added. The dissolution of marmatite was still controlled by the charge transfer process.

References

[1] WANG Jun, ZHAO Hong-bo, QIN Wen-qing, QIU Guan-zhou. Bioleaching of complex polymetallic sulfide ores by mixed culture [J]. J Cent South Univ, 2014, 21(7): 2633-2637.

[2] DEVECI H, AKCIL A, ALP I. Bioleaching of complex zinc sulphides using mesophilic and thermophilic bacteria: Comparative importance of pH and iron [J]. Hydrometallurgy, 2004, 73: 293-303.

[3] VILCAEZ J, YAMADA R, INOUE C. Effect of pH reduction and ferric ion addition on the leaching of chalcopyrite at thermophilic temperatures [J]. Hydrometallurgy, 2009, 96: 62-71.

[4] PAN Hao-dan, YANG Hong-ying, TONG Lin-lin, ZHONG Cong-bin, ZHAO Yu-shan. Control method of chalcopyrite passivation in bioleaching [J]. Transactions of Nonferrous Metals Society of China, 2012, 22(9): 2255-2260.

[5] WANG Jun, ZHU Shan, ZHANG Yan-sheng, ZHAO Hong-bo, HU Ming-hao, YANG Cong-ren, QIN Wen-qing, QIU Guan-zhou. Bioleaching of low-grade copper sulfide ores by Acidithiobacillus ferrooxidans and Acidithiobacillus thiooxidans [J]. J Cent South Univ, 2014, 21: 728-734.

[6] MOAZUR R, MUNIR A A, MAZHAR I, KALSSOM A, AHMAD M K, MUHAMMAD A G. Bioleaching of high grade Pb-Zn ore by mesophilic and moderately thermophilic iron and sulphur oxidizers [J]. Hydrometallurgy, 2009, 97: 1-7.

[7] MOUSAVI S M, YAGHMAEI S, VOSSOUGHI M, ROOSTAAZAD R, JAFARI A, EBRAHIMI M, HABIBOLLAHNIA CHABOK O, TURUNEN I. The effects of Fe(II) and Fe(III) concentration and initial pH on microbial leaching of low-grade sphalerite ore in a column reactor [J]. Bioresource Technology, 2008, 99: 2840-2845.

[8] PINA P S, LEAO V A, SILVA C A, DAMAN D, FRENAY J. The effect of ferrous and ferric iron on sphalerite bioleaching with Acidithiobacillus sp. [J]. Minerals Engineering, 2005, 18: 549-551.

[9] MEHRABANI J V, SHAFAEI S Z, NOAPARAST M, MOUSAVI S M, RAJAEI M M. Bioleaching of sphalerite sample from Kooshk lead-zinc tailing dam [J]. Transactions of Nonferrous Metals Society of China, 2013, 23(12): 3763-3769.

[10] SHI Shao-yuan, FANG Zhao-heng, NI Jin-ren. Comparative study on the bioleaching of zinc sulphides [J]. Process Biochemistry, 2006, 41: 438-446.

[11] WANG Su-ting, ZHANG Guang-ji, YUAN Qiu-hong, FANG Zhao-heng, YANG Chao. Comparative study of external addition of Fe²⁺ and inoculums on bioleaching of marmatite flotation concentrate using mesophilic and moderate thermophilic bacteria [J]. Hydrometallurgy, 2008, 93: 51-56.

[12] SHI Shao-yuan, FANG Zhao-heng. Marmatite bioleaching with moderately thermoacidophilic bacterial strain and mineral analyses of solid residues [J]. Transactions of Nonferrous Metals Society of China, 2005, 15(5): 1150-1155.

[13] XIA Jin-lan, YANG Yi, HE Huan, LIANG Chang-li, ZHAO Xiao-juan, ZHENG Lei, MA Chen-yan, ZHAO Yi-dong, NIE Zhen-yuan, QIU Guan-zhou. Investigation of the sulfur speciation during chalcopyrite leaching by moderate thermophile Sulfobacillus thermosulfidooxidans [J]. International Journal of Mineral Processing, 2010, 94: 52-57.

[14] CRUZ F L S, OLIVEIRA V A, GUIMARAES D, SOUZA A D, LEAO V. High-temperature bioleaching of nickel sulfides: Thermodynamic and kinetic implications [J]. Hydrometallurgy, 2010, 105: 103-109.

[15] OLUBAMBI P A, NDLOVU S, POTGIETER J H, BORODE J O. Role of ore mineralogy in optimizing conditions for bioleaching low-grade complex sulphide ores [J]. Transactions of Nonferrous Metals Society of China, 2008, 18(5): 1234-1246.

[16] NEMATI M, LOWENADLER J, HAPPISON S T L. Particle size effects in bioleaching of pyrite by acidophilic thermophile Sulfolobus mettallicus (BC) [J]. Applied Microbiology and Biotechnology, 2000, 53: 173-179.

[17] GONZALEZ R, GENTINA J C, ACEVEDO F. Attachment behaviour of Thiobacillus ferrooxidans cells to refractory gold concentrate particles [J]. Biotechnology Letters, 1999, 21: 715-718.

[18] DEVECI H. Effects of particle size and shape of solids on the viability of acidophilic bacteria during mixing in stirred tank reactors [J]. Hydrometallurgy, 2004, 71: 385-396.

[19] MA Peng-cheng, YANG Hong-ying, TONG Lin-lin, HAN Zhan-qi, SONG Yan. Behaviour of Fe(II) and Fe(III) in chalcopyrite bioleaching process [J]. The Chinese Journal of Nonferrous Metals, 2013, 23(6): 1694-1700. (in Chinese)

[20] SHI Shao-yuan, FANG Zhao-heng, NI Jin-ren. Electrochemistry of marmatite-carbon paste electrode in the presence of bacterial strains [J]. Bioelectrochemistry, 2006, 68(1): 113-118.

[21] GU Guo-hua, HU Ke-ting, LI Shuang-ke. Bioleaching and electrochemical properties of chalcopyrite by pure and mixed culture of Leptospirillum ferriphilum and Acidthiobacillus thiooxidans [J]. J Cent South Univ, 2013, 20: 178-183.

[22] ZHANG Yong-chun, CHEN Bu-ming, YANG Hai-tao, GUO Zhong-cheng, XU Rui-dong. Anodic behavior and microstructure of Al/Pb-Ag anode during zinc electrowinning [J]. Transactions of Nonferrous Metals Society of China, 2014, 24(3): 893-899.

[23] HANDZLIK P, FITZNER K. Corrosion resistance of Ti and Ti-Pd alloy in phosphate buffered saline solutions with and without H₂O₂ addition [J]. Transactions of Nonferrous Metals Society of China, 2013, 23(3): 866-875.

[24] BAN Jin-rong, GU Guo-hua, HU Ke-ting. Bioleaching and electrochemical property of marmatite by Leptospirillum ferrooxidans [J]. Transactions of Nonferrous Metals Society of China, 2013, 23(2): 494-500.

铁闪锌矿的Sulfobacillus thermosulfidooxidans菌浸出及电化学性能

熊先学，顾帼华，班进荣，李双棵

中南大学 资源加工与生物工程学院，长沙 410083

摘  要：采用纯种Sulfobacillus thermosulfidooxidans菌进行铁闪锌矿的生物浸出及电化学实验，研究颗粒大小、pH值控制和外加Fe³⁺离子对锌浸出的影响。结果表明：在生物浸出过程中铁闪锌矿生物浸出的最佳粒度范围为0.043~0.074 mm；定期调整pH值至初始值对获得较高的浸出率有重要影响；外加Fe³⁺离子能加速铁闪锌矿的生物浸出，但当外加Fe³⁺离子浓度超过2.5 g/L时，促进作用变弱，甚至阻碍铁闪锌矿的溶解。SEM和XRD分析浸渣发现，在矿物表面形成一层由单质硫和黄钾铁矾组成的产物层，并导致后期的浸出速度低。电化学测试实验结果表明，外加Fe³⁺离子可以增加腐蚀电流密度，有利于锌的提取。交流阻抗谱表明，添加Fe³⁺离子后没有改变反应过程的控制步骤。

关键词：铁闪锌矿；S. thermosulfidooxidans菌；生物浸出；黄钾铁矾；电化学性能

(Edited by Xiang-qun LI)

Foundation item: Project (2010CB630903) supported by the National Basic Research Program of China; Project (51374249) supported by the National Natural Science Foundation of China

Corresponding author: Xian-xue XIONG; Tel: +86-13548613068; E-mail: 369813622@qq.com

DOI: 10.1016/S1003-6326(15)63939-5

Abstract: Bioleaching and electrochemical experiments were conducted to evaluate marmatite dissolution in the presence of pure S. thermosulfidooxidans. The effects of particle size, pH controlling and external addition of Fe³⁺ ions on the zinc extraction were investigated. The results show that in the bioleaching process the best particle size range is 0.043-0.074 mm and adjusting pH regularly to the initial value has a profound effect on obtaining high leaching rate. External addition of Fe³⁺ ions could accelerate the bioleaching, while the concentration of additional Fe³⁺ over 2.5 g/L weakens the positive effect, and even hinders the dissolution of marmatite. SEM and XRD analyses of the leaching residues reveal that a product layer composed of elemental sulfur and jarosite is formed on the mineral surface, which results in a low leaching speed at later phase. The results of electrochemical measurements illustrate that additional Fe³⁺ ions could increase the corrosion current density, which is favorable to zinc extraction. The EIS spectra show that rate-limiting step does not change when Fe³⁺ ions are added.