Effects of the mineral phase and valence of vanadium on vanadium extraction from stone coal

The influence of roasting on the leaching rate and valence of vanadium was evaluated during vanadium extraction from stone coal. Vanadium in stone coal is hard to be leached and the leaching rate is less than 10% when the raw ore is leached by 4 mol/L H₂SO₄ at 90℃ for 2 h. After the sample is roasted at 900℃ for 2 h, the leaching rate of vanadium reaches the maximum, and more than 70% of vanadium can be leached. The crystal of vanadium-bearing mica minerals decomposes and the content of V(V) increases with the rise of roasting temperature from 600 to 900℃, therefore the leaching rate of vanadium increases significantly with the decomposition of the mica minerals. Some new phases, anorthite for example, form when the roasting temperature reaches 1000℃. A part of vanadium may be enwrapped in the sintered materials and newly formed phases, which may impede the oxidation of low valent vanadium and make the leaching rate of vanadium drop dramatically. The leaching rate of vanadium is not only determined by the valence state of vanadium but also controlled by the decomposition of vanadium-bearing minerals and the existence state of vanadium to a large extent.     

Experimental and theoretical studies of the reaction between cationic vanadium oxide clusters and acetylene

The time of flight mass spectrometer coupled with a laser ablation/supersonic expansion cluster source and a fast flow reactor was adopted to study the reactivity of cationic vanadium oxide clusters （VinOS,） toward acetylene （C2H2） molecules under gas phase （P, - 1.14 kPa）, under near room temperature （T, - 350 K） conditions. Association products, VmOnC2H2^＋ （m,n = 2,4; 2,6; 3,7-8; 4,9-11; 5,12-13; 6,13-16, and 7,17）, are observed. The oxidation of C2H2 by （V2Os）n^＋ （n = 1 -3） is experimentally identified. The reactivity of （V2O5）n^＋ decreases as n increases. Density functional theory （DFT） calculations were carried out to interpret the reaction mechanisms. The DFT results indicate that a terminal oxygen atom from V2O5^＋ can transfer overall barrierlessly to C2H2 at room temperature, which is in agreement with the experimental observation. Other experimental results such as the observation of V206C2H2^＋ and nonobservation of V2O7,8C2H2^＋ in the experiments are also well interpreted based on the DFT calculations. The reactivity of vanadium oxide clusters toward acetylene and other hydrocarbons may be considered in identifying molecular level mechanisms for related heterogeneous catalysis.     

Extraction of vanadium from high calcium vanadium slag using direct roasting and soda leaching

The extraction of vanadium from high calcium vanadium slag was attempted by direct roasting and soda leaching. The oxidation process of the vanadium slag at different temperatures was investigated by X-ray diffraction (XRD), scanning electron microscopy (SEM), and energy dispersive spectroscopy (EDS). The effects of roasting temperature, roasting time, Na₂CO₃ concentration, leaching temperature, leaching time, and liquid to solid ratio on the extraction of vanadium were studied. The results showed that olivine phases and spinel phases in the vanadium slag were completely decomposed at 500 and 800℃, respectively. Vanadium-rich phases were formed at above 850℃. The leaching rate of vanadium reached above 90% under the optimum conditions:roasting temperature of 850℃, roasting time of 60 min, Na₂CO₃ concentration of 160 g/L, leaching temperature of 95℃, leaching time of 150 min, and liquid to solid ratio of 10:1 mL/g. The main impurities were Si and P in the leach liquor.     

Synthesis and Structure of Polypyrrole Derivatives／V2O5 Nanocomposites

Poly ( N, N, N-trimethyl ( 2-pyrrol-l-yl ) ethyl ammonium iodide )/V2O5 ( PTPAI/V2O5) nanocomposites were synthesized by sol-gel method. This method involved formation of vanadium pentoxide xerogel in the prcscnce of polypyrrole derivatives solution. X-ray diffraction(XRD) indicated that the polypyrrole derivative particles encapsulated in the fibrous V2O5 network and the layered distance significantly increased from 1. 077 39 to 1. 354 56 nm. The interaction between polypyrrole and V2O5 in the ‘nanocomposites‘ was characterized by IR spectroscopy. The Scanning Electron Microscope(SEM) micrographs reveal the structural contrasts between the hybrid materials and the pristine vanadium oxide xerogel.     

Synthesis mechanism of LiNiVO4 by wet chemical method and mixed valence of nickel and vanadium

The single phase LiNiVO₄ has been successfully synthesized by adopting a new mild liquid route with oxalic acid as both complexant and precipitant, and this method is named the CPG method. The products were obtained by sintering the dry gel precursor which was prepared by the CPG method at 200—850℃ for 2—10 h in air. The products were tested by XRD, XPS, ESR and TGA-DTA, and the results indicate that the single phase LiNiVO₄ could be obtained at 450℃ for 2—3 h in air and LiNiVO₄ was still steady at 850℃ for 10 h. The valence analyses show that in LiNiVO₄ the valence of lithium is +1, both nickel and vanadium have the mixed valence, namely +2, +3 for nickel and +4, +5 for vanadium respectively. The LiNiVO₄ can be expressed as LiNi³⁺_xNi²⁺_1-xV⁴⁺_xV⁵⁺_1-xO₄ (0≤x<1). The pyrolysis mechanism of the dry gel is also discussed.     

Synergistic effect of microwave irradiation and CaF<Subscript>2</Subscript> on vanadium leaching

The effect and mechanism of microwave irradiation on vanadium leaching were studied via a comparison between microwave heating and conventional heating. The results show a synergistic effect of microwave irradiation and calcium fluoride (CaF₂) on the vanadium leaching efficiency. It is confirmed that the vanadium leaching process can be improved by microwave irradiation when CaF₂ is present. The leaching rate of vanadium under microwave irradiation is increased by 8%-15% when 5wt% CaF₂ is added; by contrast, in the absence of CaF₂, the leaching rate is almost unaffected compared to that by conventional heating. Morphological analysis reveals that the particles are gradually eroded by acid under microwave irradiation, whereas some of the fine particles in samples subjected to conventional heating are tightly covered by a flocculent silicate product. Moreover, a large amount of Al and V and a small amount of Si are dissolved from samples under microwave heating, as revealed by the elemental analysis of leachates. Fourier transform infrared spectroscopic analysis also indicates a higher mass transfer coefficient in the diffusion layer of the raw material by microwave irradiation. When CaF₂ is present, the reaction energy barrier is lowered and the leaching process is controlled by the tightly covered product layer, resulting in a prominent effect of microwave irradiation.     

Cyanidation of gold clay ore containing arsenic and manganese

The extraction process of gold and silver from the gold clay ore containing arsenic and manganese was investigated. With the conventional technique, the leaching rates of gold and silver are 78.23% and 49.02%, respectively. To eliminate the negative effects of arsenic and manganese on cyanidation and increase the gold and silver leaching rates, a novel catalyst was added. The content of the catalyst used in the process was 8 g per 500 g org sample, the sample size was 60 μm and the pH value was kept between 10 and 11. Leaching with the catalyst for 3–5 h under certain conditions, the gold leaching rate increased to over 90% and the silver leaching rate increased to 80%–90%. The catalyst can effectively liberate gold and silver from the enclosure of arsenic and manganese and the industrial experiment has great significance to the development and utilization of the gold clay ore containing arsenic and manganese.     

碱法浸出石煤中的钒和硅

在石煤提钒工艺中,为了充分利用石煤中的有价元素硅,采用碱浸提钒工艺提取石煤中的钒和硅.经过预焙烧后,可以有效地破坏石煤结构,提高钒硅浸出率.在焙烧温度850℃、焙烧时间2h、浸出温度95℃、浸出时间4h、固液比(g∶mL)1∶1.4、矿碱质量比1.2∶1的条件下,钒的浸出率为86.6%,硅的浸出率为61.4%.     

Comparative analysis of the dissolution kinetics of galena in binary solutions of HCl/FeCl<Subscript>3</Subscript> and HCl/H<Subscript>2</Subscript>O<Subscript>2</Subscript>

A comparative study of the dissolution kinetics of galena ore in binary solutions of FeCl₃/HCl and H₂O₂/HCl has been undertaken. The dissolution kinetics of the galena was found to depend on leachant concentration, reaction temperature, stirring speed, solid-to-liquid ratio, and particle diameter. The dissolution rate of galena ore increases with the increase of leachant concentration, reaction temperature, and stirring speed, while it decreases with the increase of solid-to-liquid ratio and particle diameter. The activation energy (E _a) of 26.5 kJ/mol was obtained for galena ore dissolution in 0.3 M FeCl₃/8.06 M HCl, and it suggests the surface diffusion model for the leaching reaction, while the E _a value of 40.6 kJ/mol was obtained for its dissolution in 8.06 M H₂O₂/8.06 M HCl, which suggests the surface chemical reaction model for the leaching reaction. Furthermore, the linear relationship between rate constants and the reciprocal of particle radius supports the fact that dissolution is controlled by the surface reaction in the two cases. Finally, the rate of reaction based on the reaction-controlled process has been described by a semiempirical mathematical model. The Arrhenius and reaction constants of 11.023 s⁻¹, 1.25×10⁴ and 3.65×10² s⁻¹, 8.02×10⁶ were calculated for the 0.3 M FeCl₃/8.06 M HCl and 8.06 M H₂O₂/8.06 M HCl binary solutions, respectively.     

微生物燃料电池用于低品位锰矿浸提的研究

为提高低品位锰矿的利用,实现有机废水对锰矿物粉的浸提,通过改造微生物燃料电池(MFC),在阴极反应池中增加电解室及矿物质室,构建用于锰矿湿法浸提的MFC反应器,实现有机废水与锰矿物粉的还原氧化反应的分离。结果显示,以乙酸钠为碳源,以低品位锰矿粉为阴极的MFC输出电压最高可达0.81 V,是以K₃[Fe(CN)₆]为阴极液(0.631 V)的1.23倍。在相同条件下,矿物浸提MFC对COD的去除率可达90.9%,高于对照组(87.5%),而降解时间为3 d,显著少于对照组(5.2 d)。在降解COD能力的提升上,可实现对低品位锰矿粉中MnO₂的还原,其锰含量由原矿粉的23%降至0.98%,浸提率可达95.7%。进一步通过高通量测序对阳极端菌群结构进行分析发现,其主要菌群为地杆菌属(Geobacter),相对于对照组的85%,矿物浸提MFC中该属比例占总菌群的95%。结果表明,矿物浸提MFC可有效地将有机降解与矿物浸提耦合,避免两者直接混合反应带来的二次废水污染及浸提产物硫酸锰的净化问题,在提高MFC产电效率、处理废水的同时,实现对低品位锰矿的浸提。     

A novel process for comprehensive utilization of vanadium slag

Traditional processes for treating vanadium slag generate a huge volume of solid residue and a large amount of harmful gas, which cause serious environmental problems. In this study, a new process for the comprehensive utilization of vanadium slag was proposed, wherein zeolite A and a V₂O₅/TiO₂ system were synthesized. The structural properties of the as-synthesized zeolite A and the V₂O₅/TiO₂ system were characterized using various experimental techniques, including X-ray diffraction, X-ray fluorescence, scanning electron microscopy, and infrared spectroscopy. The results reveal that zeolite A and the V₂O₅/TiO₂ system are successfully obtained with high purity. The results of gas adsorption measurements indicate that the prepared zeolite A exhibits high selectivity for CO₂ over N₂ and is a candidate material for CO₂ capture from flue-gas streams.     

Graded bandgap semiconductor thin film photoelectrodes

A graded bandgap oxide semiconductor thin film electrode was designed in order to obtain a photoelec-trochemically stable photoelectrode, with wide absorption range. The graded bandgap Ti_1−x V _x O₂ film electrode was prepared by heating the stacked layers of V/Ti in varying ratios, which were coated on the substrate by the sol-gel method using the starting solution with various V/Ti ratios. XPS result showed that the composition gradient was achieved for the film. The Ti_1−x V _x O₂ film electrode was found to be photoelectrochemically stable. Its photovoltage was about 360 mV. Obvious visible light photoresponse was observed for the Ti_1−x V _x O₂ film electrode. Compared with the pure TiO₂ electrode, the photocurrent onset potential of the Ti_1−x V _x O₂ film electrode was shifted positively, probably because the accumulation of vanadium at the electrode surface causes the recombination of the electrons and holes, and the lowest level of the conduction band of Ti_1−x V _x O₂ is lower than that of TiO₂. Impedance analysis showed that the donor density of the Ti_1−x V₂O₂ film electrode was higher than that of TiO₂ film electrode.     

Environmentally-friendly harvesting TiO2 nanospheres and V2O5 microrods from spent selective catalytic reduction catalysts

Spent selective catalytic reduction (SCR) catalysts are defined as hazardous wastes because of the toxicity of V₂O₅ to the ecological environment. Recycling of V₂O₅ and TiO₂ from the spent SCR catalysts has strikingly social and environmental benefits as well as economic values. In this work, a “NaOH ​+ ​Na₂CO₃” system was employed to recycle 99.2% of anatase/rutile TiO₂ nanospheres with a nanospherical morphology from the spent SCR catalysts by a simple sintering-leaching process. The observed photocatalytic performance of anatase/rutile TiO₂ nanospheres was higher than that of the other TiO₂ recovered from the spent SCR catalysts, commercial TiO₂, and chemosynthetic TiO₂, which can be ascribed to the enhanced separation of photo-excited electron/hole in a direct Z-scheme of anatase/rutile TiO₂ homostructures. Additionally, high-purity V₂O₅ microrods with high H₂S removal performance were efficiently prepared by a hydrothermal method in the leaching solution, which is superior to the traditional method including NH₄VO₃ precipitation and solvent extraction as the present method can recycle vanadate from low-grade filtrate with a 99.6% of recovery rate. This study develops an alternative method for controlling pollution of vanadate to soil and water and recycling of valuable metals.     

Modification of MgO·Al<Subscript>2</Subscript>O<Subscript>3</Subscript> spinel inclusions in Al-killed steel by Ca-treatment

The modification of MgO·Al₂O₃ spinel inclusions in Al-killed steel by Ca-treatment has been studied by industrial trials and thermodynamic calculations. In the industrial trials, samples were taken systematically during the refining process in which the molten steel was treated by calcium, and the characters of the inclusions were analyzed using scanning electron microscopy (SEM) and energy dispersive spectra (EDS). The effects of Ca-treatment were evaluated by tracking the compositions of the inclusions. The results show that the modification of MgO·Al₂O₃ spinel inclusions by Ca-treatment is effective and the transformation sequence of the inclusions during the refining is Al₂O₃→MgO·Al₂O₃→liquid complex inclusions. The modification of spinel inclusions by Ca-treatment was calculated by FactSage6.0 utilizing its free-energy minimization routines. The results of thermodynamic calculations indicate that spinel inclusions are easier to be modified than Al₂O₃ inclusions and the spinel inclusions in 30CrMo steel would transform to liquid complex inclusions when the content of dissolved Ca in the molten steel exceeds 1×10⁻⁶. Also, the results show that adding more calcium into the molten steel would lower the contents of Al₂O₃ and MgO and increase the CaO content of the inclusions, while the change in SiO₂ content is little.     

Dawson结构磷钼钒酸在环己烷催化氧化中的应用

以Dawson结构的磷钼钒杂多酸为催化剂、 质量分数为30%的H₂O₂为氧化剂, 研究环己烷的催化氧化反应. 考察了钒含量、 温度、 催化剂用量、 过氧化氢用量及反应时间对环己烷氧化反应的影响, 并将其结果与以相应的Keggin结构磷钼钒杂多酸为催化剂时得到的结果进行比较, 表明在相同反应条件下, Dawson结构的磷钼钒酸的催化活性明显高于相应的Keggin结构的磷钼钒酸的催化活性.     

CO2和O2共注入下方解石溶解对黄铁矿氧化固铀的影响

我国大型可地浸砂岩型铀矿床普遍存在黄铁矿和方解石与铀矿物密切共生现象。中性地浸采铀过程中O₂和CO₂的共注入会诱导黄铁矿氧化和方解石溶解,目前针对二者共存体系中方解石溶解对黄铁矿氧化固铀的影响尚不明确。本文通过静态批实验和数值模拟的方法对比研究了CO₂和O₂条件下方解石溶解对黄铁矿氧化固铀的影响。结果表明:无CO₂分压下中性Tris缓冲体系中黄铁矿氧化对U(VI)的吸附率高达90%,有CO₂分压下碳酸铀酰体系中铀的固定率明显降低,约有32%的铀被吸附。在方解石和黄铁矿共存体系中,单独通O₂条件下铀的吸附率为27%,CO₂和O₂共通时黄铁矿氧化对铀的吸附率仅为2%,结合数值模拟结果表明O₂₊黄铁矿+方解石体系和CO₂₊O₂₊黄铁矿+方解石体系中Ca₂(UO₂)(CO₃)₃质量比分别为80%和95%。X射线衍射(X-ray diffraction,XRD)、X射线光电子能谱(X-ray photoelectron spectroscopy,XPS)和傅里叶红外光谱(Fourier transform infrared,FT-IR)结果表明黄铁矿表面发生微氧化形成针铁矿和纤铁矿会增加U(VI)的吸附,方解石溶解促进Ca-UO₂-CO₃络合物的形成影响了黄铁矿及其氧化产物对U(VI)的固定,提高了U(VI)的迁移能力。     

高浓度NaOH浸出红土镍矿中SiO_2的研究

研究了红土镍矿高浓度NaOH浸出的条件.探讨了搅拌强度、温度、NaOH初始质量分数、浸出时间和碱矿质量比对SiO2浸出率的影响.结果表明:搅拌强度600 r/min、浸出温度225℃、初始NaOH质量分数85%、浸出时间90 min、碱矿比5∶1时,SiO2的浸出率可达82.77%.碱浸渣中的铁、镁、镍被富集,其中氧化镍的质量分数由1.29%提高到2.15%.     

A method for recovery of iron,titanium, and vanadium from vanadium-bearing titanomagnetite

An innovative method for recovering valuable elements from vanadium-bearing titanomagnetite is proposed. This method involves two procedures:low-temperature roasting of vanadium-bearing titanomagnetite and water leaching of roasting slag. During the roasting process, the reduction of iron oxides to metallic iron, the sodium oxidation of vanadium oxides to water-soluble sodium vanadate, and the smelting separation of metallic iron and slag were accomplished simultaneously. Optimal roasting conditions for iron/slag separation were achieved with a mixture thickness of 42.5 mm, a roasting temperature of 1200℃, a residence time of 2 h, a molar ratio of C/O of 1.7, and a sodium carbonate addition of 70wt%, as well as with the use of anthracite as a reductant. Under the optimal conditions, 93.67% iron from the raw ore was recovered in the form of iron nugget with 95.44% iron grade. After a water leaching process, 85.61% of the vanadium from the roasting slag was leached, confirming the sodium oxidation of most of the vanadium oxides to water-soluble sodium vanadate during the roasting process. The total recoveries of iron, vanadium, and titanium were 93.67%, 72.68%, and 99.72%, respectively.     

Microstructure evolution and phase transformation of traditional cast and spray-formed hypereutectic aluminium-silicon alloys induced by heat treatment

Microstructural evolution and phase transformation induced by different heat treatments of the hypereutectic aluminium-silicon alloy, Al-25Si-5Fe-3Cu (wt%, signed as 3C), fabricated by traditional cast (TC) and spray forming (SF) processes, were investigated by differential scanning calorimetry (DSC) and scanning electron microscopy (SEM) combined with energy dispersive X-ray spectroscopy and X-ray diffraction techniques. The results show that Al₇Cu₂Fe phase can be formed and transformed in TC- and SF-3C alloys between 802–813 K and 800–815 K, respectively. The transformation from β-Al₅FeSi to δ-Al₄FeSi₂ phase via peritectic reaction can occur at around 858–870 K and 876–890 K in TC- and SF-3C alloys, respectively. The starting precipitation temperature of δ-Al₄FeSi₂ phase as the dominant Fe-bearing phase in the TC-3C alloy is 997 K and the exothermic peak about the peritectic transformation of δ-Al₄FeSi₂→β-Al₅FeSi is not detected in the present DSC experiments. Also, the mechanisms of the microstructural evolution and phase transformation are discussed.     

钒渣钙化焙烧的影响因素及焙烧氧化动力学

采用钙化焙烧方式处理转炉钒渣以提高钒的浸出率,考察了焙烧参数(渣样粒度,升温速率,焙烧保温温度及保温时间,配钙量)对钒浸出率的影响,根据钒渣氧化的TG-DSC曲线对钒渣氧化变温动力学进行了分析.结果表明:降低升温速率可提高钒氧化率,保温温度高于600℃时钒浸出率迅速增加.在钒渣粒径48~75μm,外配钙m(CaO)/m(V2O5)为042,升温速率2℃·min-1,保温温度850℃,保温时间150min的条件下,钒浸出率达9331%.钒尖晶石氧化过程受三级化学反应控制,升温速率为5和10℃·min-1的表观活化能分别为26765,25603kJ·mol-1.