In order to extract gallium from a high-silica-content flue dust generated in corundum production,a mixed acid solution of H2SO4 and HF was used for leaching,and test parameters of the leaching process were optimized....In order to extract gallium from a high-silica-content flue dust generated in corundum production,a mixed acid solution of H2SO4 and HF was used for leaching,and test parameters of the leaching process were optimized.Experimental results show that the leaching rate of gallium was only 38%when H2SO4 was used as leaching agent.Composition analysis results of micro areas in this corundum flue dust indicate that the content of gallium in silica-enriched phases was high;this portion of gallium was insoluble in H2SO4 solution.The leaching rate of gallium increased significantly with addition of HF due to corrosion of silica.Effects of reaction time,temperature,and concentrations of HF and H2SO4 on leaching rates of gallium were investigated.The leaching rate of gallium reached 91%when this corundum flue dust was leached in a mixed acid solution of H2SO4 and HF for 4 h,at a temperature of 80°C,with a liquid-to-solid ratio of 5:1(mL/g).The optimal concentrations of H2SO4 and HF in the mixed acid solution were 1.5 and 6.4 mol/L,respectively.展开更多
To investigate the physical and chemical properties of the steelmaking dust, wet sieve separation, XRD, SEM, EDS, and traditional chemical analysis were carded out to obtain the particle size distribution, mineralogy,...To investigate the physical and chemical properties of the steelmaking dust, wet sieve separation, XRD, SEM, EDS, and traditional chemical analysis were carded out to obtain the particle size distribution, mineralogy, morphology, and the chemical composition of the dust. The dust with a total Fe content of 64.08wt% has coarse metallic iron, magnetite and hematite grains, while free clay minerals with a size of 〈38 μm are mainly iosidefite, calcium silicate, and calcite, which are conglomerated to each other. By following the procedures of wet magnetic separation, acid leaching, and oxidization calcination, magnetic materials were recycled and further prepared as iron oxide red with a productivity of 0.54 ton per unit ton of the dust. Middle iron concentrate with an Fe content of 65.92wt% can be reused as feeding material in the ironmaking industry. Additionally, washed water from acid leaching with an Fe^3＋ ion content of less than 5 g·L^-1 was recovered as feeding water in the wet magnetic separation procedure. 2008 University of Science and Technology Beijing. All fights reserved.展开更多
In order to remove phosphorus element from steelmaking slag and decrease iron loss,malic acid was selected as the leaching agent to dissolve steelmaking slag.Firstly,the influences of different factors,such as malic a...In order to remove phosphorus element from steelmaking slag and decrease iron loss,malic acid was selected as the leaching agent to dissolve steelmaking slag.Firstly,the influences of different factors,such as malic acid concentration,slag particle size,temperature,liquid/solid ratio and stirring speed,on the leaching ratios of phosphorus and iron were studied.Then,the kinetics for the leaching process of phosphorus was analyzed.The results showed that the leaching ratios of phosphorus and iron increase significantly with increasing the malic acid solution concentration and liquid/solid ratio.When the concentration of malic acid solution increases up to 0.01492 mol/L,about 80%phosphorus can be dissolved,and iron leaching ratio is less than 17%.In addition,decreasing slag particle size can obviously increase the leaching ratio of phosphorus.However,temperature and stirring speed have no significant effect on the dissolution of phosphorus and iron.The leaching kinetics of phosphorus follows the unreacted shrinking core model.Diffusion through product layer is the rate-limiting step of the leaching process,and the corresponding apparent activation energy is determined to be 3.32 kJ/mol.Finally,a semi-empirical kinetic equation was established.展开更多
为研究高炉瓦斯泥硫酸浸出锌过程的动力学,以河北某高炉瓦斯泥为原料进行了硫酸浸出试验,分别考察了浸出温度、硫酸浓度对浸出过程锌浸出率的影响。随着浸出温度的升高和硫酸浓度的增加,锌浸出率逐渐提高,浸出速率降低。采用Avrami动力...为研究高炉瓦斯泥硫酸浸出锌过程的动力学,以河北某高炉瓦斯泥为原料进行了硫酸浸出试验,分别考察了浸出温度、硫酸浓度对浸出过程锌浸出率的影响。随着浸出温度的升高和硫酸浓度的增加,锌浸出率逐渐提高,浸出速率降低。采用Avrami动力学模型对锌浸出过程进行模拟,结果表明,浸出过程符合n=0.160 4的Avrami动力学模型,反应表观活化能为10.02 k J/mol,说明浸出过程受扩散控制,因此要提高浸出效率,应加强扩散效应。提高硫酸浓度或升高反应温度,加速了溶液中的反应过程和传质过程,锌浸出率提高。试验结果为湿法浸出过程动力学以及固废资源化利用后续研究和生产实践提供了一定的理论依据。展开更多
河北某瓦斯泥锌含量为8.74%、铁品位为27.4%,含锌矿物主要为红锌矿,含铁矿物主要为赤铁矿。为回收瓦斯泥中锌等有价元素,对其进行了硫酸浸出试验。结果表明,常温下,硫酸浓度为0.5 mol/L、液固比为6 m L/g、反应时间为15 min、搅拌速度为...河北某瓦斯泥锌含量为8.74%、铁品位为27.4%,含锌矿物主要为红锌矿,含铁矿物主要为赤铁矿。为回收瓦斯泥中锌等有价元素,对其进行了硫酸浸出试验。结果表明,常温下,硫酸浓度为0.5 mol/L、液固比为6 m L/g、反应时间为15 min、搅拌速度为300 r/min条件下,可以获得锌浸出率为95.21%的指标,浸渣中锌品位降至0.5%。试验结果可以为该类瓦斯泥矿硫酸溶解浸出提供技术依据。展开更多
基金Projects(51274240,51204209)supported by the National Natural Science Foundation of China
文摘In order to extract gallium from a high-silica-content flue dust generated in corundum production,a mixed acid solution of H2SO4 and HF was used for leaching,and test parameters of the leaching process were optimized.Experimental results show that the leaching rate of gallium was only 38%when H2SO4 was used as leaching agent.Composition analysis results of micro areas in this corundum flue dust indicate that the content of gallium in silica-enriched phases was high;this portion of gallium was insoluble in H2SO4 solution.The leaching rate of gallium increased significantly with addition of HF due to corrosion of silica.Effects of reaction time,temperature,and concentrations of HF and H2SO4 on leaching rates of gallium were investigated.The leaching rate of gallium reached 91%when this corundum flue dust was leached in a mixed acid solution of H2SO4 and HF for 4 h,at a temperature of 80°C,with a liquid-to-solid ratio of 5:1(mL/g).The optimal concentrations of H2SO4 and HF in the mixed acid solution were 1.5 and 6.4 mol/L,respectively.
文摘To investigate the physical and chemical properties of the steelmaking dust, wet sieve separation, XRD, SEM, EDS, and traditional chemical analysis were carded out to obtain the particle size distribution, mineralogy, morphology, and the chemical composition of the dust. The dust with a total Fe content of 64.08wt% has coarse metallic iron, magnetite and hematite grains, while free clay minerals with a size of 〈38 μm are mainly iosidefite, calcium silicate, and calcite, which are conglomerated to each other. By following the procedures of wet magnetic separation, acid leaching, and oxidization calcination, magnetic materials were recycled and further prepared as iron oxide red with a productivity of 0.54 ton per unit ton of the dust. Middle iron concentrate with an Fe content of 65.92wt% can be reused as feeding material in the ironmaking industry. Additionally, washed water from acid leaching with an Fe^3＋ ion content of less than 5 g·L^-1 was recovered as feeding water in the wet magnetic separation procedure. 2008 University of Science and Technology Beijing. All fights reserved.
基金This work was financially supported by the National Natural Science Foundation of China(52074004 and 51604003)Director Fund of Anhui Province Key Laboratory of Metallurgical Engineering and Resources Recycling(Anhui University of Technology)and Anhui Special Support Plan(T000609).
文摘In order to remove phosphorus element from steelmaking slag and decrease iron loss,malic acid was selected as the leaching agent to dissolve steelmaking slag.Firstly,the influences of different factors,such as malic acid concentration,slag particle size,temperature,liquid/solid ratio and stirring speed,on the leaching ratios of phosphorus and iron were studied.Then,the kinetics for the leaching process of phosphorus was analyzed.The results showed that the leaching ratios of phosphorus and iron increase significantly with increasing the malic acid solution concentration and liquid/solid ratio.When the concentration of malic acid solution increases up to 0.01492 mol/L,about 80%phosphorus can be dissolved,and iron leaching ratio is less than 17%.In addition,decreasing slag particle size can obviously increase the leaching ratio of phosphorus.However,temperature and stirring speed have no significant effect on the dissolution of phosphorus and iron.The leaching kinetics of phosphorus follows the unreacted shrinking core model.Diffusion through product layer is the rate-limiting step of the leaching process,and the corresponding apparent activation energy is determined to be 3.32 kJ/mol.Finally,a semi-empirical kinetic equation was established.
文摘为研究高炉瓦斯泥硫酸浸出锌过程的动力学,以河北某高炉瓦斯泥为原料进行了硫酸浸出试验,分别考察了浸出温度、硫酸浓度对浸出过程锌浸出率的影响。随着浸出温度的升高和硫酸浓度的增加,锌浸出率逐渐提高,浸出速率降低。采用Avrami动力学模型对锌浸出过程进行模拟,结果表明,浸出过程符合n=0.160 4的Avrami动力学模型,反应表观活化能为10.02 k J/mol,说明浸出过程受扩散控制,因此要提高浸出效率,应加强扩散效应。提高硫酸浓度或升高反应温度,加速了溶液中的反应过程和传质过程,锌浸出率提高。试验结果为湿法浸出过程动力学以及固废资源化利用后续研究和生产实践提供了一定的理论依据。
