Oxidation kinetics of ilmenite concentrate by non-isothermal thermogravimetric analysis

IF 3.1 2区 材料科学 Q1 METALLURGY & METALLURGICAL ENGINEERING Journal of Iron and Steel Research(International) Pub Date : 2017-07-01 DOI:10.1016/S1006-706X(17)30102-4
Ying-yi Zhang , Wei Lv , Xue-wei Lv , Chen-guang Bai , Ke-xi Han , Bing Song
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引用次数: 13

Abstract

The non-isothermal oxidation experiments of ilmenite concentrate were carried out at various heating rates under air atmosphere by thermogravimetry. The oxidation kinetic model function and kinetic parameters of apparent activation energy (Ea) were evaluated by Málek and Starink methods. The results show that under air atmosphere, the oxidation process of ilmenite concentrate is composed of three stages, and the chemical reaction (G(α) = 1—(1—α)2, where α is the conversion degree) plays an important role in the whole oxidation process. At the first stage (α = 0. 05–0. 30), the oxidation process is controlled gradually by secondary chemical reaction with increasing conversion degree. At the second stage (α = 0.30–0.50), the oxidation process is completely controlled by the secondary chemical reaction (G(α) = 1 – (1 – α)2). At the third stage (α=0. 50 – 0.95), the secondary chemical reaction weakens gradually with increasing conversion degree, and the oxidation process is controlled gradually by a variety of functions; the kinetic equations are G(α)–(1–α)−1 (ß=10 K · min−1, where ß is heating rate), G(α) = (1 – α) −½ (ß= 15 – 20 K · min−1), and G(α) = (1 – α)−2(ß=25 K · min−1), respectively. For the whole oxidation process, the activation energies follow a parabolic law with increasing conversion degree, and the average activation energy is 160. 56 kJ · mol−1.

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钛铁矿精矿的非等温热重分析氧化动力学
采用热重法对钛铁矿精矿在空气气氛下不同升温速率下的非等温氧化进行了实验研究。采用Málek和Starink方法对氧化动力学模型函数和表观活化能(Ea)动力学参数进行了评价。结果表明:在空气气氛下,钛铁矿精矿氧化过程分为3个阶段,其中化学反应(G(α) = 1 - (1 - α)2,其中α为转化度)在整个氧化过程中起重要作用。在第一阶段(α = 0。05-0。30)随着转化程度的增加,氧化过程由二次化学反应逐渐控制。在第二阶段(α = 0.30-0.50),氧化过程完全由二次化学反应(G(α) = 1 - (1 - α)2)控制。在第三阶段(α=0。50 ~ 0.95),随着转化程度的增加,二次化学反应逐渐减弱,氧化过程逐渐受到多种功能的控制;动力学方程G(α)-(1 -α)−1(ß= 10 K·分钟−1,ß升温速率),G(α)=(1 -α)−½(ß= 15 - 20 K·分钟−1),和G(α)=(1 -α)−2(ß= 25 K·分钟−1),分别。整个氧化过程的活化能随转化率的增加呈抛物线规律,平均活化能为160。56 kJ·mol−1。
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来源期刊
CiteScore
4.30
自引率
0.00%
发文量
2879
审稿时长
3.0 months
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