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Oxidative desulfurization of dibenzothiophene over V-Mo co-doped akaganeite
Journal of Environmental Chemical Engineering ( IF 7.4 ) Pub Date : 2024-09-26 , DOI: 10.1016/j.jece.2024.114267 Shengguo Zhang, Xiaodong Wang, Qiuye Li, Jianjun Yang
Journal of Environmental Chemical Engineering ( IF 7.4 ) Pub Date : 2024-09-26 , DOI: 10.1016/j.jece.2024.114267 Shengguo Zhang, Xiaodong Wang, Qiuye Li, Jianjun Yang
In this paper, V-Mo co-doped akaganeite (β-FeOOH) was prepared by one-pot hydrothermal method and the oxidative desulfurization (ODS) of dibenzothiophene over the catalyst was carefully investigated. 0.07 g (ca. 0.35 wt% of model oil) of catalyst induced 100 % of DBT removal in 60 min with a O/S of 20:1 under 60 °C for the model oils with any of the sulfur contents, 100 ppm, 500 ppm, or 1000 ppm. Moreover, the DBT removal after recycling 4 times is still 100 % and it only declines to 98.04 % in the fifth cycle, which indicates that the catalyst has a good stability and recycling performance. Doping V species in Mo doped β-FeOOH not only initiates a micro-variation in catalyst structure and the resultant more active •OH species but also forms a more stable structure of the catalyst, enabling the catalyst to exhibit a higher ODS reaction rate and a better reusability. The GC-MS analyses demonstrated that the DBT was converted to DBTO2 by two steps: (1) DBT→ DBTO; (2) DBTO→ DBTO2, and the former is the rate-limiting step.
中文翻译:
V-Mo 共掺杂赤金石上二苯并噻吩的氧化脱硫
本文采用一锅水热法制备了 V-Mo 共掺杂赤金石 (β-FeOOH),并仔细研究了二苯并噻吩在催化剂上的氧化脱硫 (ODS)。0.07 g(约 0.35 wt% 的模型油)催化剂可在 60 分钟内诱导 100% 的 DBT 去除,对于 60 °C 下硫含量为 100 ppm、500 ppm 或 1000 ppm 的模型油,O/S 为 20:1。此外,回收 4 次后的 DBT 去除率仍然是 100%,在第 5 次循环中仅下降到 98.04%,这表明催化剂具有良好的稳定性和回收性能。Mo 掺杂 β-FeOOH 中的掺杂 V 物质不仅引发了催化剂结构的微变化,从而产生了更活跃的 •OH 物质,而且还形成了更稳定的催化剂结构,使催化剂表现出更高的 ODS 反应速率和更好的可重用性。GC-MS 分析表明,DBT 通过两个步骤转换为 DBTO2:(1) DBT→ DBTO;(2) DBTO→ DBTO2,前者是限流步骤。
更新日期:2024-09-26
中文翻译:
V-Mo 共掺杂赤金石上二苯并噻吩的氧化脱硫
本文采用一锅水热法制备了 V-Mo 共掺杂赤金石 (β-FeOOH),并仔细研究了二苯并噻吩在催化剂上的氧化脱硫 (ODS)。0.07 g(约 0.35 wt% 的模型油)催化剂可在 60 分钟内诱导 100% 的 DBT 去除,对于 60 °C 下硫含量为 100 ppm、500 ppm 或 1000 ppm 的模型油,O/S 为 20:1。此外,回收 4 次后的 DBT 去除率仍然是 100%,在第 5 次循环中仅下降到 98.04%,这表明催化剂具有良好的稳定性和回收性能。Mo 掺杂 β-FeOOH 中的掺杂 V 物质不仅引发了催化剂结构的微变化,从而产生了更活跃的 •OH 物质,而且还形成了更稳定的催化剂结构,使催化剂表现出更高的 ODS 反应速率和更好的可重用性。GC-MS 分析表明,DBT 通过两个步骤转换为 DBTO2:(1) DBT→ DBTO;(2) DBTO→ DBTO2,前者是限流步骤。