Recovery of indium and lead from lead bullion

Lead and indium were recovered by electrolysis and nonequilibrium solvent extraction process from lead bullion.The effects of current density,electrolytic period and circle amnant of electrolyte on the electrochemical dissolution of lead and indium were investigated.The effects of extraction phase ratio and mixing time on solvent extraction of indium and striping phase ratio and stripping stage on the loaded organic phase stripping were also investigated.The experimental results indicate that under optimum conditions,the purity of lead deposited on cathode is 98.5% and the deposit rate of lead is 99.9%,the dissolution rate of indium is 94.28%,the extraction rate of indium is 98.69%,the stripping rate of indium is almost 100%,and the impurity elements,such as Zn,Fe and Sn can be removed.     

Extraction of nickel from molybdenum leaching residue of metalliferous black shale by segregation roasting and acid leaching

The recovery of nickel from molybdenum leach residue by the process of segregation roasting-sulfuric acid leaching-solvent extraction was investigated. The residue was characterized by microscopic investigations, using X-ray fluorescence spectrometry (XRF) and X-ray diffractometry (XRD) techniques and the residue after segregation roasting was characterized by chemical phase analysis method. A series of experiments were conducted to examine the mass ratio of activated carbon (AC) to the residue, segregation roasting time and temperature, sulfuric acid concentration, liquid-to-solid ratio, leaching time, leaching temperature, addition amount of 30% H₂O₂, stirring speed (a constant) on the leaching efficiency of nickel. A maximum nickel leaching efficiency of 90.5% is achieved with the mass ratio of AC to the residue of 1:2.5, segregation roasting time of 2 h, segregation roasting temperature of 850 °C, sulfuric acid concentration of 4.5 mol/L, liquid-to-solid ratio of 6:1, leaching time of 5 h, leaching temperature of 80 °C, addition of 30% H₂O₂ of 0.6 mL for 1 g dry residue. Under these optimized conditions, the average leaching efficiency of nickel is 89.3%. The nickel extraction efficiency in the examined conditions is about 99.6%, and the nickel stripping efficiency in the examined conditions is about 99.2%.     

Recovery of molybdenum from residues by simultaneous ultrafine milling and alkali leaching

A new technology of treating molybdenum residues by simultaneous ultmfme milling and alkali leaching was put forward to recover molybdenum from metallurgical residues. The effects of residue size, milling time, solid content, n(Na2CO3)/n(Mo) and slurry pH value on molybdenum leaching rate were investigated. The results indicate that a simpler process, lower slurry temperature, 50% shorter treating time, 60% decrease of Na2CO3 content and 15% increase of molybdenum leaching rate can be obtained by the new technology compared with the traditional process. The leaching kinetic equation was determined, and calculation of active energy (E = 56.2 kJ/mol) shows that the leaching process of molybdenum residues by simultaneous ultmfine milling and alkali leaching is controlled by chemical reaction. Potential exists for the new process to form the basis for an economically viable, environmentally friendly process to recover valuable elements from residues.     

Extracting indium and preparing ferric oxide for soft magnetic ferrite materials from zinc calcine reduction lixivium

A hydrometallurgical process for indium extraction and ferric oxide powder preparation for soft magnetic ferrite material was developed.Using reduction lixivium from high-acid reductive leaching of zinc oxide calcine as raw solution,copper and indium were firstly recovered by iron powder cementation and neutralization.The recovery ratios of Cu and In are 99% and 95%,respectively.Some harmful impurities that have negative influences on magnetic properties of soft magnetic ferrite material are deeply removed ...     

机械活化法强化液晶显示器中铟浸出的动力

以废液晶显示器(Liquid Crystal Display,LCD)面板为原料,介绍了利用机械活化手段强化LCD面板中铟浸出的方法,研究了机械活化法对浸出铟的影响,以及活化后浸出铟的动力学规律。研究结果表明,机械活化法可有效强化LCD中铟的浸出反应。物料经机械活化后,化学活性提高,反应速度加快,表观活化能和表观反应级数均降低。活化30和60 min后的浸铟表观活化能由未活化时的70.2 k J/mol分别降低至53.3和39.7 k J/mol,表观反应级数由原来的1.21分别降低至0.98和0.89。     

Leaching kinetics of low grade zinc oxide ore in NH3-NH4Cl-H2O system

The leaching kinetics of low grade zinc oxide ore in NH3-NH4Cl-H2O system was studied. The effects of ore particle size, reaction temperature and the sum concentration of ammonium ion and ammonia on the leaching efficiency of zinc were examined. The leaching kinetics of low-grade zinc oxide ore in NH3-NH4Cl-H2O system follows the kinetic law of shrinking-core model. The results show that diffusion through the inert particle pores is the leaching kinetics rate controlling step. The calculated apparent activation energy of the process is about 7.057 kJ/mol. The leaching efficiency of zinc is 92.1% under the conditions of ore particle size of 69μm, holding at 80℃ for 60 min, sum ammonia concentration of 7.5 mol/L, the molar ratio of ammonium to ammonia being 2：1, and the ratio （g/mL） of solid to liquid being 1：10.     

Preparation ＆ Properties Research of Two Indium Phthalocyanine Materials

Two iodo（phthalocyainato） indium complexes were synthesized and mixed with polymer solution（PMMA/chloroform）to prepare iodo（phthalocyainato）indium/PMMA compound film materials on a glass slice by the method of dipping film.Two materials have typical B-band and Q-band absorption of Phthalocyanine compounds in the UV-Vis spectrum.The reverse saturable absorption experiments show that two materials have better reverse saturable absorption properties while they have higher linear transmissivity.In addition,the highest transmittance of visible light is over 70%（tetrakis（cumylphenoxy）phthalocyainate indium/OMMA compound film material）.The initial threshold is 127.1mJ/cm^2.The dynamic range is 1.43.It can be concluded that introduction of the substituted groups having bigger steric hindrance and conjugative effect in the Phthalocyanine ring may increase the reverse saturable absorption effect of the Phthalocyanine indium material.     

Dissolution kinetics of malachite in ammonia/ammonium sulphate solution

The dissolution kinetics of malachite was investigated in ammonia/ammonium sulphate solution. The effects of ammonia and ammonium sulphate concentration, pH, leaching time, reaction temperature, and particle size were determined. The results show that the optimum leaching conditions for malachite ore with a copper extraction more than 96.8% are ammonia/ammonium concentration 3.0 mol/L NH₄OH + 1.5 mol/L (NH₄)₂SO₄, liquid-to-solid ratio 25:1 mL/g, leaching time 120 min, stirring speed 500 r/min, reaction temperature 25 °C and particle size finer than 0.045 mm. The dissolution process of malachite with an activation energy of 26.75 kJ/mol is controlled by the interface transfer and diffusion across the product layer. A semi-empirical rate equation is obtained to describe the leaching process and the reaction orders with respect to concentration of ammonia and ammonium sulphate are 2.983 0 and 0.941 1, respectively.     

Extracting gold from pyrite roster cinder by ultra-fine-grinding and resin-in-pulp

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Kinetics of nickel leaching from roasting-dissolving residue of spent catalyst with sulfuric acid

Sulfuric acid leaching process was applied to extract nickel from roasting-dissolving residue of a spent catalyst, the effect of different parameters on nickel extraction was investigated by leaching experiments, and the leaching kinetics of nickel was analyzed. The experimental results indicate that the effects of particle size and sulfuric acid concentration on the nickel extraction are remarkable; the effect of reaction temperature is mild; while the effect of stirring speed in the range of 400–1 200 r/min is negligible. Decreasing particle size or increasing sulfuric acid concentration and reaction temperature, the nickel extraction efficiency is improved. 93.5% of nickel in residue is extracted under suitable leaching conditions, including particle size (0.074–0.100) mm, sulfuric acid concentration 30% (mass fraction), temperature 80 °C, reaction time 180 min, mass ratio of liquid to solid 10 and stirring speed 800 r/min. The leaching kinetics analyses shows that the reaction rate of leaching process is controlled by diffusion through the product layer, and the calculated activation energy of 15.8 kJ/mol is characteristic for a diffusion controlled process. Foundation item: Project (50574101) supported by the National Natural Science Foundation of China; Project (2003UDBEA00C020) supported by the Collaborative Project of School and Province of Yunnan Province, China     

Mechanism of crud formation in copper solvent extraction

The authors investigated the mechanism of crud formation in copper solvent extraction. It is indicated that pH value of solution and the phase ratio (O/A) are the main factors affecting crud formation in solvent extraction. The amount of crud extraction increases with aqueous pH value increase, and reduces with the increase of the phase ratio. Fe3 , Mg2 , fine air bubble and suspended particulates in leaching solution contribute to crud formation. One case is that a series of reactions of hydrolization and polymerization occurs for Fe3 , while pH＞2.5, polyhydric complex or Fe-SO4 complex are formed. Then the complex-ions of FeOH2 , Fe2(OH)4 2 cause poly-reaction, which is likely to lead emulsion. The study on Zeta potential indicates the repulsion between electriferous droplets in solvent extraction prevents phase coalescence, which is one of the major reasons for emulsion.     

Concentrating Ge in zinc hydrometallurgical process with hot acid leaching-halotrichite method

1　INTRODUCTIONInthezincconcentratesfromHuidongLead zincMinelocatedinsouth westofChina ,therearerichraremetalssuchasGewhichhasverywideapplica tionsandhighvalue .However ,Gewaslargelywast edbecauseitwasdispersedinalotofresidues(halotrichiteresidue ,Ge Feresidueandhighacidleachedresidue)intheconventionalzinchydrometal lurgicalprocessforthezincconcentrates[1] .InordertoconcentrateandrecoverGe ,anovelhydrometal lurgicalprocess ,ie ,thehotacidleaching halotrichitemethodofzinchasbeendevelope…     

Extraction separation of germanium with hydroxamic acid HGS98

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SELECTIVE DISSOLUTION OF GOLD IN AN ALKALINETHIOUREA SOLUTION BY ELECTROLYSIS

Thioureawaswellknownasanlixiviantforgoldearlyin1932[fi.Thedissolutionofgoldinacidicthioureasolutionwasreportedin1941byPlaksin[Zj.Thioureahasbeenwidelypaidattentiontoasahighselectivenontoxicnovellixiviantofgoldsince197013j.Electrochemicalexperimentsongoldelectrodeshavebeenconductedbymanyresearches,showingthatgolddissolutionbythioureaismoreefficientinacidicsolutionthaninneutralandalkalinesolutions[4j.Theprocessforextract'inggoldfromtheoreorscrapbyacidicthioureasolution,however,demandedexcessive…     

STUDY ON TREATMENT OF AMMONIA LEACHING SLAG IN THE METALLURGICAL PROCESS OF TUNGSTEN

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含钒灰渣酸浸提钒工艺酸浸条件的试验研究

含钒灰渣中钒的酸浸效率直接影响了整个提钒工艺中钒的总回收率,同时,酸浸条件对钒的酸浸效率有着显著的影响作用.为获取含钒灰渣酸浸提钒工艺酸浸阶段的工艺条件,及含钒灰渣的酸浸特性,在对灰渣中钒的赋存状态进行全面分析的基础上,针对硫酸浓度、酸浸温度、酸浸时间和液固比等酸浸影响因素,在实验室分别进行了酸浸条件试验研究;分析酸浸液、酸浸残渣的成分,计算得到V2O5酸浸效率.试验结果表明:酸浸温度和硫酸浓度对酸浸效率起主要影响作用.合理工艺条件为:硫酸浓度为5.0～6.0mol/L,酸浸温度为115～120℃,酸浸时间为6h左右,液固比为2.5∶1～3∶1.在此条件下,V2O5酸浸效率达到85%以上.     

氯化浸出铅阳极泥回收金的研究

试验对湿法处理铅阳极泥回收金进行了研疣．实验结果表明：铜的浸出是酸浸除杂的主要影响因素,在温度为65℃,盐酸浓度为2．9moL／L,氯化钠浓度为1．3mol／L,硫酸浓度为0．3mol／L时,铜的浸出率达到92．03％,杂质能有效去除．在氯化浸金的过程中,温度与氯酸钠的用量对金的浸出率影响最大．随着两者的增加,金的浸出率将明显地增加．当温度大于80℃,氯酸钠用量大于料重的12．5％,硫酸浓度为1．5mol／L时,金的浸出率大于98％．     

Selective leaching of vanadium from V-Ti magnetite concentrates by pellet calcification roasting-H_2SO_4 leaching process

A novel method of pellet calcification roasting-H_2 SO_4 leaching was proposed to efficiently separate and extract vanadium(V) from vanadium-titanium(V-Ti) magnetite concentrates.The leaching rate of V is as high as 88.98%,while the leaching rate of impurity iron is only 1.79%.Moreover,the leached pellets can be used as raw materials for blast furnace ironmaking after secondary roasting.X-ray photoelectron spectroscopy(XPS) and scanning electron microscopy with energy dispersive X-ray spectrometry(SEMEDS) analyses showed that V~(3+) was oxidized to V~(5+) after roasting at 1200℃,and V~(5+) was then leached by H_2 SO_4.X-ray diffraction(XRD) analyses and single factor experiment revealed a minimal amount of dissolved Fe_2 O_3 during H_2 SO_4 leaching.Therefore,a high separation degree of V and iron(Fe) from V-Ti magnetite concentrate was achieved through H_2 SO_4 leaching.Compared with the traditional roastingleaching process,this process can achieve a high selectivity of V and Fe,and has excellent prospects for industrial production.     

甲基磺酸- 双氧水体系对印刷电路板拆解技术

废印刷电路板上元器件的拆解技术是电路板资源化再利用的重要环节。通过研究甲基磺酸-双氧水体系下元器件的脱落率,得出优化的实验条件为:甲基磺酸浓度范围为3.0～3.5 mol/L,双氧水浓度范围为0.4～0.6 mol/L,反应时间45 min。在该实验条件下,实验样品中焊接元器件脱落率达到100%,实现了电路板基板与元器件的快速高效分离,为废旧电路板上元器件的拆解技术提供一定的技术支撑。     

Simultaneous electrogenerative leaching of chaicopyrite concentrate and MnO2

In order to enhance the electrogenerative leaching rate of chalcopyrite concentrate reasonably, the principle of generative process was applied to simultaneous leaching of chalcopyrite concentrate and MnO2. The results show that Cu^2＋ and Mn^2＋ in addition to electrical energy could be acquired in the simultaneous electrogenerative leaching process. The leaching cell has the open circuit potential of about 1.0 V and gains quantity of electricity of about 700 C. The optimum leaching rates of Cu^2＋ and Mn^2＋ are 23.10% and 22.1%, respectively after electrogenera- tive leaching for about 10 h under the present conditions.