化学
活化能
阿累尼乌斯方程
吸附
吸附
活性炭
解吸
动力学
吸附剂
离子交换
碳纤维
电解质
铼
速率决定步骤
反应速率常数
无机化学
杂质
离子
物理化学
催化作用
有机化学
复合数
电极
物理
材料科学
量子力学
复合材料
作者
Karolina Kołczyk-Siedlecka,Robert P. Socha,Xuegeng Yang,Kerstin Eckert,Marek Wojnicki
出处
期刊:Hydrometallurgy
[Elsevier BV]
日期:2022-10-21
卷期号:215: 105973-105973
被引量:7
标识
DOI:10.1016/j.hydromet.2022.105973
摘要
This paper presents the potential use of carbon sorbents in recovering rhenium(VII) from highly diluted electrolytes. Tests were performed using synthetic solutions containing selenium(VI) as an impurity. Adsorption of Re(VII) is selective with respect to selenium(VI). Activated carbon is a suitable sorbent for rhenium recovery because unlike ion-exchange resins, it has high chemical resistance and osmotic-shock resistance. The results show that the sorption mechanism is complex. Two follow-up processes occurred—physical adsorption and the reduction of Re(VII) to Re(VI). The processes were strongly influenced by the temperature. The lower the temperature, the higher the process efficiency. The observed sorption capacity was as high as 7.6 mg/g at 298 K and decreased as the temperature increased. The adsorption was a mixed-control process. Increasing the temperature altered the rate-limiting process. The activation parameters were determined using rate constant (k) and Arrhenius equation. In the first step, the activation energy was approximately 0 kJ mol−1. In the second step, the activation energy for k2,obs and k3,obs was determined as 57.3 kJ mol−1. The pre-exponential factors were calculated; their value was 2.98 × 107 min−1. For k1,obs, the activation energy was nearly 0 kJ mol−1.
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