Prekob Ádám, Udayakumar Mahitha, Karacs Gábor, Kristály Ferenc, Muránszky Gábor, Leskó Anett Katalin, Németh Zoltán, Viskolcz Béla, Vanyorek László
Institute of Chemistry, University of Miskolc, H-3515 Miskolc-Egyetemváros, Hungary.
Advanced Materials and Intelligent Technologies Higher Education and Industrial Cooperation Centre, University of Miskolc, H-3515 Miskolc-Egyetemváros, Hungary.
Nanomaterials (Basel). 2021 Apr 29;11(5):1172. doi: 10.3390/nano11051172.
Glassy carbon foam (GCF) catalyst supports were synthesized from waste polyurethane elastomers by impregnating them in sucrose solution followed by pyrolysis and activation (AC) using N and CO gas. The palladium nanoparticles were formed from Pd(NO). The formed palladium nanoparticles are highly dispersive because the mean diameters are 8.0 ± 4.3 (Pd/GCF), 7.6 ± 4.2 (Pd/GCF-AC1) and 4.4 ± 1.6 nm (Pd/GCF-AC2). Oxidative post-treatment by CO of the supports resulted in the formation of hydroxyl groups on the GCF surfaces, leading to a decrease in zeta potential. The decreased zeta potential increased the wettability of the GCF supports. This, and the interactions between -OH groups and Pd ions, decreased the particle size of palladium. The catalysts were tested in the hydrogenation of nitrobenzene. The non-treated, glassy-carbon-supported catalyst (Pd/GCF) resulted in a 99.2% aniline yield at 293 K and 50 bar hydrogen pressure, but the reaction was slightly slower than other catalysts. The catalysts on the post-treated (activated) supports showed higher catalytic activity and the rate of hydrogenation was higher. The maximum attained aniline selectivities were 99.0% (Pd/GCF-AC1) at 293 K and 98.0% (Pd/GCF-AC2) at 323 K.
玻璃碳泡沫(GCF)催化剂载体由废弃聚氨酯弹性体制备而成,具体方法是将其浸渍在蔗糖溶液中,随后进行热解,并使用氮气和一氧化碳气体进行活化(AC)。钯纳米颗粒由硝酸钯(Pd(NO))形成。所形成的钯纳米颗粒具有高度分散性,因为其平均直径分别为8.0±4.3(Pd/GCF)、7.6±4.2(Pd/GCF - AC1)和4.4±1.6纳米(Pd/GCF - AC2)。载体经一氧化碳氧化后处理导致GCF表面形成羟基,从而使zeta电位降低。降低的zeta电位增加了GCF载体的润湿性。这以及-OH基团与钯离子之间的相互作用减小了钯的粒径。对这些催化剂进行了硝基苯加氢测试。未经处理的玻璃碳负载催化剂(Pd/GCF)在293 K和50巴氢气压力下苯胺产率为99.2%,但反应速度比其他催化剂稍慢。后处理(活化)载体上的催化剂表现出更高的催化活性,加氢速率更高。在293 K时,最大苯胺选择性为99.0%(Pd/GCF - AC1),在323 K时为98.0%(Pd/GCF - AC2)。