Extraction and kinetic analysis of Pb and Sr from the leaching residue of zinc oxide ore

NH_4HCO_3 conversion followed by HCl leaching was performed and proven to be effective in extracting Pb and Sr from zinc extracted residual. The mechanism and operating conditions of NH_4HCO_3 conversion, including molar ratio of NH_4HCO_3 to zinc extracted residual,NH_4HCO_3 concentration, conversion temperature, conversion time, and stirring velocity, were discussed, and operating conditions were optimized by the orthogonal test. Experimental results indicate that NH_4HCO_3 conversion at temperatures ranging from 25 to 85°C follows the shrinking unreacted core model and is controlled by inner diffusion through the product layer. The extraction ratios of Pb and Sr under optimized conditions reached 85.15% and 87.08%, respectively. Moreover, the apparent activation energies of Pb and Sr were 13.85 and13.67 k J·mol~(-1), respectively.     

Reaction condition optimization and kinetic investigation of roasting zinc oxide ore using (NH<Subscript>4</Subscript>)<Subscript>2</Subscript>SO<Subscript>4</Subscript>

An orthogonal test was used to optimize the reaction conditions of roasting zinc oxide ore using (NH₄)₂SO₄. The optimized reaction conditions are defined as an (NH₄)₂SO₄/zinc molar ratio of 1.4:1, a roasting temperature of 440°C, and a thermostatic time of 60 min. The molar ratio of (NH₄)₂SO₄/zinc is the most predominant factor and the roasting temperature is the second significant factor that governs the zinc extraction. Thermogravimetric–differential thermal analysis was used for (NH₄)₂SO₄ and zinc mixed in a molar ratio of 1.4:1 at the heating rates of 5, 10, 15, and 20 K·min-1. Two strong endothermic peaks indicate that the complex chemical reactions occur at approximately 290°C and 400°C. XRD analysis was employed to examine the transformations of mineral phases during roasting process. Kinetic parameters, including reaction apparent activation energy, reaction order, and frequency factor, were calculated by the Doyle–Ozawa and Kissinger methods. Corresponding to the two endothermic peaks, the kinetic equations were obtained.     

Thermodynamics and phase transformations in the recovery of zinc from willemite

Willemite is a common component of zinc and lead metallurgical slags that, in the absence of effective utilization methods, cause serious environmental problems. To solve this problem and increase zinc recovery, we proposed a novel extraction method of zinc from willemite by calcified roasting followed by leaching in NH₄Cl-NH₃·H₂O solution. The thermodynamics and phase conversion of Zn₂SiO₄ to zinc oxide (ZnO) during calcified roasting with CaO were investigated. The mechanism of mineralogical phase conversion and the effects of the CaO-to-Zn₂SiO₄ mole ratio (n(CaO)/n(Zn₂SiO₄)), roasting temperature, and the roasting time on zinc-bearing phase conversion were experimentally investigated. The results show that Zn₂SiO₄ was first converted to Ca₂ZnSi₂O₇ and then to ZnO. The critical step in extracting zinc from willemite is the conversion of Zn₂SiO₄ to ZnO. The zinc percent leached in the ammonia leaching system rapidly increased because of the gradual complete phase conversion from willemite to ZnO via the calcified roasting process.     

(NH4)2SO4焙烧?浸出法从氧化锌矿石中提取锌

An improved method of (NH₄)₂SO₄ roasting followed by water leaching to utilize zinc oxidized ores was studied. The operating parameters were obtained by investigating the effects of the molar ratio of (NH₄)₂SO₄ to zinc, roasting temperature, and holding time on zinc extraction. The roasting process followed the chemical reaction control mechanism with the apparent activation energy value of 41.74 kJ·mol?1. The transformation of mineral phases in roasting was identified by X-ray diffraction analysis combined with thermogravimetry–differential thermal analysis curves. The water leaching conditions, including the leaching temperature, leaching time, stirring velocity, and liquid-to-solid ratio, were discussed, and the leaching kinetics was studied. The reaction rate was obtained under outer diffusion without product layer control; the values of the apparent activation energy for two stages were 4.12 and 8.19 kJ·mol?1. The maximum zinc extraction ratio reached 96% while the efficiency of iron extraction was approximately 32% under appropriate conditions. This work offers an effective method for the comprehensive use of zinc oxidized ores.     

Thermodynamics and kinetics of extracting zinc from zinc oxide ore by the ammonium sulfate roasting method

Thermodynamic analyses and kinetic studies were performed on zinc oxide ore treatment by (NH₄)₂SO₄ roasting technology. The results show that it is theoretically feasible to realize a roasting reaction between the zinc oxide ore and (NH₄)₂SO₄ in a temperature range of 573-723 K. The effects of reaction temperature and particle size on the extraction rate of zinc were also examined. It is found that a surface chemical reaction is the rate-controlling step in roasting kinetics. The calculated activation energy of this process is about 45.57 kJ/mol, and the kinetic model can be expressed as follows:1-(1-α)1/3=30.85 exp(-45.57/RT)·t. An extraction ratio of zinc as high as 92% could be achieved under the optimum conditions.     

铁酸锌焙烧后的还原行为及氨浸特性

A novel method for recovering zinc from zinc ferrite by reduction roasting–ammonia leaching was studied in this paper. The reduction thermodynamic of zinc ferrite by CO was analyzed. The effects of roasting parameters on the phase transformation and conversion rate of zinc ferrite, and the leaching behavior of zinc from the reductive roasted samples by ammonia leaching, were experimentally investigated. The mineralogical phase compositions and chemical compositions of the samples were characterized by X-ray diffraction and chemical titration methods, respectively. The results showed that most of the zinc ferrite was transformed to zinc oxide and magnetite after weak reduction roasting. 86.43% of the zinc ferrite was transformed to zinc oxide under the optimum conditions: CO partial pressure of 25%, roasting temperature of 750°C, and roasting duration of 45 min. Finally, under the optimal leaching conditions, 78.12% of zinc was leached into the solution from the roasted zinc ferrite while all iron-bearing materials were kept in the leaching residue. The leaching conditions are listed as follows: leaching duration of 90 min, ammonia solution with 6 mol/L concentration, leaching temperature of 50°C, solid-to-liquid ratio of 40 g/L, and stirring speed of 200 r/min.     

Characteristics of the reduction behavior of zinc ferrite and ammonia leaching after roasting

A novel method for recovering zinc from zinc ferrite by reduction roasting–ammonia leaching was studied in this paper. The reduction thermodynamic of zinc ferrite by CO was analyzed. The effects of roasting parameters on the phase transformation and conversion rate of zinc ferrite, and the leaching behavior of zinc from the reductive roasted samples by ammonia leaching, were experimentally investigated. The mineralogical phase compositions and chemical compositions of the samples were characterized by X-ray diffraction and chemical titration methods, respectively. The results showed that most of the zinc ferrite was transformed to zinc oxide and magnetite after weak reduction roasting. 86.43% of the zinc ferrite was transformed to zinc oxide under the optimum conditions: CO partial pressure of 25%, roasting temperature of 750°C, and roasting duration of 45 min. Finally, under the optimal leaching conditions, 78.12% of zinc was leached into the solution from the roasted zinc ferrite while all iron-bearing materials were kept in the leaching residue. The leaching conditions are listed as follows: leaching duration of 90 min,ammonia solution with 6 mol/L concentration, leaching temperature of 50°C, solid-to-liquid ratio of 40 g/L, and stirring speed of 200 r/min.     

Efficient and selective recovery of Ni,Cu, and Co from low-nickel matte via a hydrometallurgical process

Low-nickel matte was intensively characterized, and Ni, Cu, and Co were determined to exist mainly as (Fe,Ni)₉S₈ and FeNi₃, Cu₅FeS₄, and (Fe,Ni)₉S₈ and Fe₃O₄ (in isomorphic form), respectively. The efficient and selective extraction of Ni, Cu, and Co from the low-nickel matte in an (NH₄)₂S₂O₈/NH₃·H₂O solution system was studied. The effects of (NH₄)₂S₂O₈ and NH₃·H₂O concentrations, leaching time, and leaching temperature on the metal extraction efficiency were systematically investigated. During the oxidative ammonia leaching process, the metal extraction efficiencies of Ni 81.07%, Cu 93.81%, and Co 71.74% were obtained under the optimal conditions. The relatively low leaching efficiency of Ni was mainly ascribed to NiFe alloy deactivation in ammonia solution. By introducing an acid pre-leaching process into the oxidative ammonia leaching process, we achieved the high extraction efficiencies of 98.03%, 99.13%, and 85.60% for the valuable metals Ni, Cu, and Co, respectively, from the low-nickel matte.     

Effect of modifying agents on the hydrophobicity and yield of zinc borate synthesized by zinc oxide

The aim of this study was to synthesize zinc borate using zinc oxide, reference boric acid, and reference zinc borate (reference ZB) as the seed, and to investigate the effects of modifying agents and reaction parameters on the hydrophobicity and yield, respectively. The reaction parameters include reaction time (1–5 h), reactant ratio (H₃BO₃/ZnO by mass: 2–5), seed ratio (seed crystal/(H₃BO₃+ZnO) by mass: 0–2wt%), reaction temperature (50–120℃), cooling temperature (10–80℃), and stirring rate (400–700 r/min); the modifying agents involve propylene glycol (PG, 0–6wt%), kerosene (1wt%–6wt%), and oleic acid (OA, 1wt%–6wt%) with solvents (isopropyl alcohol (IPA), ethanol, and methanol). The results of reaction yield obtained from either magnetically or mechanically stirred systems were compared. Zinc borate produced was characterized by X-ray diffraction (XRD), Fourier transform infrared spectroscopy (FT-IR), and contact angle tests to identify the hydrophobicity. In conclusion, zinc borate is synthesized successfully under the optimized reaction conditions, and the different modifying agents with various solvents affect the hydrophobicity of zinc borate.     

Preparation of ultrafine silica from potash feldspar using sodium carbonate roasting technology

A novel process was developed for the preparation of ultrafine silica from potash feldspar. In the first step, potash feldspar was roasted with Na₂CO₃ and was followed by leaching using NaOH solution to increase the levels of potassium, sodium, and aluminum in the solid residue. The leaching solution was then carbonated to yield ultrafine silica. The optimized reaction conditions in the roasting process were as follows: an Na₂CO₃-to-potash feldspar molar ratio of 1.1, a reaction temperature of 875°C, and a reaction time of 1.5 h. Under these conditions, the extraction rate of SiO₂ was 98.13%. The optimized carbonation conditions included a final solution pH value of 9.0, a temperature of 40°C, a CO₂ flow rate of 6 mL/min, a stirring intensity of 600 r/min, and an ethanol-to-water volume ratio of 1:9. The precipitation rate and granularity of the SiO₂ particles were 99.63% and 200 nm, respectively. We confirmed the quality of the obtained ultrafine silica by comparing the recorded indexes with those specified in Chinese National Standard GB 25576―2010.     

低品位氧化锌矿湿法浸取制备纳米氧化锌

以低品位氧化锌矿为原料,通过酸浸、净化除杂得到纯净的硫酸锌溶液.以碳酸氢铵为沉淀剂,采用直接沉淀法制备纳米氧化锌粉体.考察了碳酸氢铵和硫酸锌的物质的量之比、反应温度、反应时间、前驱体碱式碳酸锌的热分解温度及时间对纳米氧化锌粒径大小及锌沉淀率或产品纯度的影响.采用X射线衍射仪、扫描电子显微镜等对产品的粒径及晶型结构进行检测.结果表明,所得产品为六方晶系氧化锌,形貌为球状,平均粒径为40 nm,ZnO质量分数达到97.5%.所设计工艺可得到技术指标达到GB/T 19589-2004 国家标准中纳米氧化锌粉体要求,且操作简便易行,易于工业化生产.     

利用高效溶磷菌钝化修复铅污染土壤效果及其影响因素研究

利用高效溶磷菌的溶磷特性对受铅污染土壤展开修复研究,研究了菌液添加量与土壤全磷含量对重度污染土壤修复效果的影响。通过测定有效磷含量、有效态铅含量、pH等指标变化,结合X射线衍射法(XRD)分析土壤物相变化,初步研究了溶磷菌的钝化机制。当目标溶磷菌发酵菌液的添加量达到150mL/kg时,目标菌可有效在土壤中存活;当土壤全磷含量达到1g/kg时,经过钝化培养可将土壤有效态铅含量降至4mg/kg、土壤中有效磷含量增加至19mg/kg。对钝化后土壤Pb形态分析表明,在目标溶磷菌作用下,土壤中Pb由可交换态、碳酸盐结合态向残渣态转变,XRD分析结果表明残渣态主要为氯磷酸铅盐化合物(Pb_5(PO_4)_3Cl),是Pb在土壤中最稳定的化合物之一。     

纳米Cu/γ-Al_2O_3催化剂制备与选择催化还原NO性能

采用NH4Al(SO4)2、NH4HCO3和NH3.H2O为原料沉淀制备γ-Al2O3,然后浸渍负载活性组分Cu2+,制成纳米Cu/γ-Al2O3催化剂,并考察其催化性能.SEM测试结果表明:制得的纳米Cu/γ-Al2O3催化剂粒径均小于100 nm.活性测试结果表明:在pH值为8.5时制备的γ-Al2O3负载上3%Cu2+的纳米Cu/γ-Al2O3催化剂性能最佳,在275℃时能使NO的转化率达到82.3%,与普通Cu/γ-Al2O3催化剂相比较,最佳活性温度降低了25℃,NO最大转化率提高了31.8%.     

化学沉淀法制备超细先驱沉淀物

研究了以铝铵钒和碳酸氢铵为原料 ,采用化学沉淀法制备尺寸均一、颗粒细小分散的碱式碳酸铝铵先驱沉淀物的工艺 研究表明反应物的混合方式对先驱沉淀物的尺寸和形貌有很大的影响 采用先缓慢滴加 ,在反应物充分混合且过饱和度达到一定程度的基础上 ,再将沉淀剂雾化加入的工艺有利于得到分散、尺寸均一细小的NH4Al(OH) 2 CO3先驱沉淀物 ,为纳米级氧化铝粉体的制备提供了基础     

锌浸出渣的还原焙烧和人工硫化矿物浮选过程中硫酸铅和硫酸锌的反应行为

To evaluate the feasibility of recovering Pb and Zn sulfides and Ag-containing minerals from Zn leaching residue by the process of reduction roasting followed by flotation, the reaction behaviors of Pb and Zn sulfates during this process were investigated. Chemical analysis showed that the transformation ratios of PbSO₄ and ZnSO₄ could reach 65.51% and 52.12%, respectively, after reduction roasting, and the introduction of a sulfidation agent could improve the transformation ratios of these sulfates. scanning electron microscopy–energy dispersive spectroscopy (SEM–EDS) revealed that temperature obviously affects the particle size, crystal growth, and morphology of the artificial Pb and Zn sulfide minerals. Particle size analysis demonstrated that the particle size of the materials increases after roasting. Flotation tests revealed that a flotation concentrate composed of 12.01wt% Pb, 27.78wt% Zn, and 6.975 × 10?2wt% Ag with recoveries of 60.54%, 29.24%, and 57.64%, respectively, could be obtained after roasting.     

二氧化硫脲合成工艺的改进

以工业级过氧化氢为氧化剂,研究硫脲氧化合成二氧化硫脲的工艺条件．重点考察了反应温度、氧化剂及其稳定剂、瘩剂用量、反应时间和投料配比等因素对目标产物产率的影响;在优化条件下,氧化产率达到85％本法具有氧化活性高、稳定性好、水溶液体系可重复使用,无腐蚀性、无污染等突出优点,     

沉淀除杂法提高稀土纯度的研究

本文以氨水和碳酸氢铵为联合除杂剂、对粗产品混合稀土氧化物进行了纯化研究。可将混合稀土氧化物(RE2O3)含量从92%左右提高到98%以上。铝的含量可降至万分之几,铁可降至十万分之几。     

硫氧混合铅锌矿中锌的氧化氨浸动力学

常压低温条件下在NH3-(NH4)2 SO4体系中使用过硫酸铵作为氧化剂对硫氧混合铅锌矿中的锌进行浸出实验,系统研究了搅拌速度、浸出剂浓度、氧化剂浓度与温度对于锌浸出率的影响.结果表明,在最优条件下锌的浸出率可达93.2%,且浸出过程中几乎没有其他离子进入溶液,实现了锌的选择性高效浸出,从而简化了后续的浸出液净化与材料制备过程.动力学研究表明,硫氧混合铅锌矿中锌的氧化氨浸过程遵循固体产物层扩散控制的未反应核收缩模型,浸出反应的表观活化能为17.89 kJ·mol-1.     

粘土固化注浆帷幕对有害物质的阻滞作用

分析了粘土固化注浆结石体对固体废物填埋场渗滤液中有害物质的阻滞效果．采用高浓度、高水头梯度条件下的重金属离子和有机物对4cm厚的结石体进行渗流实验．研究结果表明由Pb     

微波消解—石墨炉原子吸收光谱法测定鱼丸中的铅、镉含量

采用微波消解法处理样品,石墨炉原子吸收光谱法测定铅镉含量,用磷酸二氢铵和硝酸镁混合溶液作为基体改进剂消除干扰。在优化的试验条件下,测得铅、镉检出限分别为0.052mg/kg、0.004mg/kg;相对标准偏差为（n=6）1.57%～4.39%、2.26%～3.13%;回收率为96.5%～104.0%、95.0%～103.3%。