Praserthdam Supareak, Rittiruam Meena, Maungthong Kanokpon, Saelee Tinnakorn, Somdee Siriwimol, Praserthdam Piyasan
High-Performance Computing Unit (CECC-HCU), Center of Excellence on Catalysis and Catalytic Reaction Engineering (CECC), Chulalongkorn University, Bangkok, 10330, Thailand.
Center of Excellence on Catalysis and Catalytic Reaction Engineering (CECC), Chulalongkorn University, Bangkok, 10330, Thailand.
Sci Rep. 2020 Nov 3;10(1):18952. doi: 10.1038/s41598-020-76094-2.
The catalytic performance with high conversion and high selectivity of Ti-based oxide catalysts have been widely investigated. Besides, stability, which is an essential parameter in the industrial process, lacked fundamental understanding. In this work, we combined computational and experimental techniques to provide insight into the deactivation of P25 and TS-1 Ti-based oxide catalysts during the methyl oleate (MO) epoxidation. The considered deactivation mechanisms are fouling and surface oxygen vacancy (O). The fouling causes temporary catalyst deactivation through active site blockage but can be removed via calcination in air at high temperature. However, in this work, the O formation plays an important role in the overall performance of the spent catalyst as the deactivated catalyst after regeneration, cannot be restored to the initial activity. Also, the effects of O in spent catalysts caused (i) the formation of more Ti species on the surface as evident by XPS and Bader charge analysis, (ii) the activity modification of the active region on the catalyst surface as the reduction in energy gap (E) occurred from the formation of the interstates observed in the density of states profiles of spent catalyst modeled by the O-vacant P25 and TS-1 models. This reduction in E affects directly the strength of Ti-OOH active site and MO bonding, in which high binding energy contributes to a low conversion because the MO needed an O atom from Ti-OOH site to form the methyl-9,10-epoxy stearate. Hence, the deactivation of the Ti-based oxide catalysts is caused not only by the insoluble by-products blocking the active region but also mainly from the O. Note that the design of reactive and stable Ti-based oxide catalysts for MO epoxidation needed strategies to prevent O formation that permanently deactivated the active region. Thus, the interrelation and magnitude between fouling and O formation on catalyst deactivation will be investigated in future works.
钛基氧化物催化剂具有高转化率和高选择性的催化性能已得到广泛研究。此外,稳定性作为工业过程中的一个重要参数,人们对其缺乏基本的了解。在这项工作中,我们结合计算和实验技术,以深入了解在油酸甲酯(MO)环氧化过程中P25和TS-1钛基氧化物催化剂的失活情况。所考虑的失活机制是结垢和表面氧空位(O)。结垢通过活性位点堵塞导致催化剂暂时失活,但可通过在空气中高温煅烧去除。然而,在这项工作中,O的形成在失活催化剂再生后的整体性能中起着重要作用,因为再生后的失活催化剂无法恢复到初始活性。此外,失活催化剂中O的影响导致:(i)XPS和巴德电荷分析表明表面形成了更多的钛物种;(ii)催化剂表面活性区域的活性发生改变,这是由于通过O空位P25和TS-1模型模拟的失活催化剂的态密度分布中观察到的能隙(E)减小所致。E的这种减小直接影响Ti-OOH活性位点与MO键合的强度,其中高结合能导致转化率低,因为MO需要来自Ti-OOH位点的一个O原子来形成9,10-环氧硬脂酸甲酯。因此,钛基氧化物催化剂的失活不仅是由于不溶性副产物堵塞了活性区域,还主要是由于O。需要注意的是,用于MO环氧化的活性和稳定的钛基氧化物催化剂的设计需要防止O形成的策略,因为O的形成会使活性区域永久失活。因此,未来的工作将研究结垢与O形成对催化剂失活的相互关系和程度。