首页> 外文期刊>Journal of Mining and Metallurgy, Section B: Metallurgy >Thermodynamic and kinetics analysis of the sulfur-fixed roasting of antimony sulfide using ZnO as sulfur-fixing agent
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Thermodynamic and kinetics analysis of the sulfur-fixed roasting of antimony sulfide using ZnO as sulfur-fixing agent

机译:ZnO作为固硫剂对硫化锑进行固硫焙烧的热力学和动力学分析

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Currently, the commercial antimony metallurgy is mainly based on pyrometallurgical processes and oxidative volatilization of Sb2S3 is an essential step. This step includes the problems of high energy consumption and low concentration of SO2 pollution. Aiming at these problems, we present a new method of sulfur-fixing roasting of antimony sulfide. This method uses ZnO as a sulfur-fixing agent, and roasting with Sb2S3 was carried out at 673 K~1073 K to produce Sb2O3 and ZnS. By calculating the thermodynamics of the reactions, we can conclude that the Gibbs Free Energy Change (ΔGθ) of roasting reaction is below -60 kJ/mol and the predominance areas of Sb2O3 and ZnS are wide and right shifting with the temperature increase, which all indicates that this method is theoretically feasible. The reacted products between Sb2S3 and ZnO indicated that the reaction began at 773 K and finished approximately at 973K. We used the Ozawa-Flynn-Wall, Kissinger and Coats-Redfern method to calculate the kinetics of the roasting reaction. The conclusion is as follows: The average values of apparent activation energy (E) and natural logarithmic frequency factor (lnA) calculated by Ozawa-Flynn-Wall, Kissinger and Coats-Redfern were 189.72 kJ·mol-1 and 35.29 s-1, respectively. The mechanism of this reaction was phase boundary reaction model. The kinetic equation is shown as follow, where α represents reaction fraction: 1-(1-α)1/3 = 2.12 x1015 exp(-1.90x105/RT) t.
机译:当前,商业锑冶金主要基于火法冶金工艺,Sb2S3的氧化挥发是必不可少的步骤。该步骤包括高能耗和SO 2污染浓度低的问题。针对这些问题,我们提出了一种硫化锑固硫焙烧的新方法。该方法使用ZnO作为固硫剂,在673 K〜1073 K的温度下用Sb2S3焙烧,生成Sb2O3和ZnS。通过计算反应的热力学,我们可以得出结论,焙烧反应的吉布斯自由能变化(ΔGθ)低于-60 kJ / mol,并且随着温度的升高,Sb2O3和ZnS的主要区域宽而右移,所有这些表明该方法在理论上是可行的。 Sb2S3和ZnO之间的反应产物表明,反应在773 K处开始,大约在973 K处结束。我们使用Ozawa-Flynn-Wall,Kissinger和Coats-Redfern方法来计算焙烧反应的动力学。结论如下:Ozawa-Flynn-Wall,Kissinger和Coats-Redfern计算的视在活化能(E)和自然对数频率因子(lnA)的平均值为189.72 kJ·mol-1和35.29 s-1,分别。该反应的机理是相边界反应模型。动力学方程如下所示,其中α表示反应分数:1-(1-α)1/3 = 2.12 x1015 exp(-1.90x105 / RT)t。

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