Acidithiobacillus ferrooxidans-硫酸酸溶联合浸出金川铜镍硫化矿尾矿砂实验研究

金川铜镍硫化矿尾矿砂富含Cu、Ni和Co等金属,为对其进行回收,对新尾矿库不同深度的尾矿砂分别进行了直接硫酸酸溶浸出与A.f.-硫酸酸溶联合浸出实验,利用ICP-AES分析了不同阶段浸出液中Cu2+、Ni2+、Co2+含量。实验结果表明,A.f.-硫酸酸溶联合浸出工艺对尾矿砂中有价金属Cu、Ni和Co的浸出效果优于单独酸溶浸出工艺。其中,A.f.-硫酸酸溶联合浸出法对1m深度的尾矿砂中Cu、Ni、Co的浸出率最高,分别达到95.78%、98.01%和75.13%,而单独硫酸酸溶作用的离子浸出率分别为75.69%、74.33%和42.33%。

铜渣中有价金属酸溶出试验研究

利用硫酸溶出铜渣中的有价元素,研究了常压下硫酸体积分数、浸出时间、浸出温度和硫酸用量(固/液比)对铜渣中Fe、Cu、Co和Ni的溶出率及溶出速率的影响。结果表明:随着硫酸体积分数的升高,促进了硅酸凝胶在酸液中的形成,吸附浸出液中的金属离子,导致了溶液中各金属的溶出率有所降低;浸出温度的升高有助于提高铜渣中金属元素的溶出率。通过试验研究获得了铜渣中有价金属浸出的最佳条件:硫酸体积分数20%,硫酸用量为理论用量的7倍,浸出温度90℃,浸出时间2 h,此条件下Fe、Cu、Co和Ni的溶出率分别达到94.5%、69.7%、73.9%、36.4%。

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.

Precipitation of antimony from the solution of sodium thioantimonite by air oxidation in the presence of catalytic agents

The behavior of antimony oxidation in the solution of sodium thioantimonite was studied in the presence of catalytic agents. The catalytic effects of the respective addition of cupric sulfate, sodium tartrate, potassium permanganate, phenol, 1,2 dihydroxybenzene and their combination on the oxidation of sodium thioantimonite were investigated. A pilot test was carried out. The results show that the respective use of sodium tartrate, cupric sulfate, potassium permanganate, phenol and 1,2 dihydroxybenzene have little catalytic effect on the oxidation of sodium thioantimonite. However there exists obvious catalytic oxidation by the combination of 0.25 g/L 1,2 dihydroxybenzene, 0.5 g/L potassium permanganate and 1.0 g/L phenol. Moreover, high blast intensity, the increase of temperature and NaOH concentration favor the oxidation of antimony. The oxidation process of antimony has such advantages as quick reaction and low operation costs. The results of the pilot test are consistent with those of laboratory experiments.

脱硫石膏与柠檬酸渣在水泥生产中的应用比较

本文通过对比试验研究了脱硫石膏对水泥物理性能的影响。研究结果表明:不同厂家的脱硫石膏以及柠檬酸渣对水泥物理性能尤其是抗压强度的影响较大。通过原因分析,判断硫酸根溶出速率是主要影响因素。针对这一影响因素,在大磨生产试验中进一步进行验证,并通过降低细度控制指标来提高脱硫石膏的溶出速率,从而降低其对水泥强度的影响,以判断其生产应用的可行性。

Leaching kinetics of molybdenum from Ni-Mo ore in sulfuric acid solution with sodium peroxodisulfate as oxidant

The leaching kinetics of molybdenum from Ni-Mo ore in sulfuric acid solution with sodium peroxodisulfate was studied.The effects including leaching temperature, reaction time, particle size, stirring speed, and concentrations of sulfuric acid and sodium peroxodisulfate were investigated. The leaching process of molybdenum from Ni-Mo ore is controlled by the chemical reaction through the solid layer across the unreacted shrinking core. The apparent activation energy of the leaching of molybdenum is calculated to be 41.0 k J/mol and the leaching kinetics equation of molybdenum from Ni-Mo ore is expressed as1-(1-a)1/3=3405.7exp[-41030.0/(RT)]t.

Mechanism of Chalcopyrite Leaching in Oxidative Sulphuric Acid Solution

The mechanism of the leaching process of chalcopyrite concentrate with sodium nitrate in sulphuric acid solution were studied and discussed. Chemical reactions of leaching and their thermodynamic probabilities are predicted based on the calculated Gibbs energies and analysis of E-pH diagrams. Experimental data, thermodynamic analysis, chemical, XRD, and SEM/EDX analyses of concentrate and the leach residues, were performed to develop a better understanding of the chemical reactions that took place in the system. Elemental sulphur was formed as the main leaching product, precipitated at the particle surfaces and tended to inhibit the leaching rate.

Mechanism study on the effect of different surfactants on dissolution rate of recrystallized prednisolone in various concentrations

The effects of re-crystallization of prednisolone as a poorly water-soluble drug in aqueous surfactant solutions on its dissolution rate were investigated. A significant enhancement was observed for crystal dissolution rate in hydrophilic surfactants such as tween 80 and sodium lauryl sulfate （SLS）. Differential scanning calorimetry （DSC） and Fourier transform infrared spectroscopy （FT-IR） indicated the existence of both form Ⅰ and Ⅱ ofprednisolone in SLS treated crystals. The FT-IR results also showed that, only form Ⅱ could be detected in prednisolone crystals without surfactant and prednisolone form Ⅲ was produced in tween 80 treated crystals. These results were also confirmed by X-ray （XRD） diffraction and scanning electron microscopy （SEM）. In general, the results indicated that the presence of hydrophilic surfactants could generate forms Ⅱ and Ⅲ of the crystals. These forms would give rlse to the increase of prednisolone＇s dissolution rate owing to their physicochemical instability and more hydrophilic property in comparison with stable polymorph of form Ⅰ.