Vaidulych Mykhailo, Yeh Li-Ya, Hoehner Robin, Jašík Juraj, Kadam Shashikant A, Vorochta Michael, Khalakhan Ivan, Hagen Jan, Vajda Štefan
Department of Nanocatalysis, J. Heyrovský Institute of Physical Chemistry, v.v.i., Czech Academy of Sciences, Dolejškova 2155/3, CZ-182 23 Prague 8, Czech Republic.
Saint-Gobain Research Germany, Glasstraße 1, 52134 Herzogenrath, Germany.
J Phys Chem C Nanomater Interfaces. 2024 Feb 16;128(8):3180-3192. doi: 10.1021/acs.jpcc.3c07064. eCollection 2024 Feb 29.
Films of titania-supported monometallic Pd, Pt, and bimetallic Pt-Pd catalysts made of metallic nanoparticles were prepared by magnetron sputtering and studied in the oxidative dehydrogenation (ODH) of cyclohexene. Pd/TiO and Pt-Pd/TiO were found active at as low temperature as 150 °C and showed high catalytic activity with high conversion (up to 81%) and benzene selectivity exceeding 97% above 200 °C. In turn, the Pt/TiO catalyst performed poorly with the onset of benzene production at 200 °C only and conversions not exceeding 5%. The activity of bimetallic Pt-Pd catalysts far exceeded all of the other investigated catalysts at temperatures below 250 °C. However, the production of benzene significantly dropped with a further temperature increase due to the enhanced combustion of CO at the expense of benzene formation. As in situ NAP-XPS measurement of the Pt-Pd/TiO catalyst in the reaction conditions of the ODH of cyclohexene revealed Pd surface enrichment during the first temperature ramp, we assume that Pd surface enrichment is responsible for enhanced activity at low temperatures in the bimetallic catalyst. At the same time, the Pt constituent contributes to stronger cyclohexene adsorption and oxygen activation at elevated temperatures, leading to changes in conversion and selectivity with a drop in benzene formation and increased combustion to CO. Both the monometallic Pd and the Pt-Pd-based catalysts produced a small amount of the second valuable product, cyclohexadiene, and below 250 °C produced only a negligible amount of CO (<0.2%). To summarize, Pd- and Pt-Pd-based catalysts were found to be promising candidates for highly selective low-temperature dehydrogenation of cyclic hydrocarbons that showcased reproducibility and stability after the temperature activation. Importantly, these catalysts were fabricated by utilizing proven methods suitable for large-scale production on extended surfaces.
通过磁控溅射制备了由金属纳米颗粒制成的二氧化钛负载单金属钯、铂以及双金属铂 - 钯催化剂薄膜,并在环己烯的氧化脱氢(ODH)反应中进行了研究。发现Pd/TiO₂ 和Pt - Pd/TiO₂ 在低至150℃时具有活性,在200℃以上表现出高催化活性,转化率高(高达81%)且苯选择性超过97%。相比之下,Pt/TiO₂ 催化剂性能较差,仅在200℃时开始产生苯,转化率不超过5%。在低于250℃的温度下,双金属Pt - Pd催化剂的活性远远超过所有其他研究的催化剂。然而,随着温度进一步升高,由于以苯的形成为代价增强了CO的燃烧,苯的产量显著下降。由于在环己烯ODH反应条件下对Pt - Pd/TiO₂ 催化剂进行原位NAP - XPS测量发现在第一次升温过程中钯表面富集,我们认为钯表面富集是双金属催化剂在低温下活性增强的原因。同时,铂组分有助于在高温下更强的环己烯吸附和氧活化,导致转化率和选择性发生变化,苯的形成减少且燃烧生成CO增加。单金属钯和基于Pt - Pd的催化剂都产生少量的第二种有价值的产物环己二烯,并且在250℃以下仅产生可忽略量的CO(<0.2%)。总之,发现基于钯和Pt - Pd的催化剂是环状烃高选择性低温脱氢的有前途的候选者,在温度活化后具有可重复性和稳定性。重要的是,这些催化剂是通过适用于在扩展表面上大规模生产的成熟方法制备的。