Abstract:This work reports the preparation of a La2O3‐modified Pt/TiO2 (Pt/La‐TiO2) hybrid through an excess‐solution impregnation method and its application for CO2 hydrogenation catalysis. The Pt/La‐TiO2 catalyst is characterized by XRD, H2 temperature‐programmed reduction (TPR), TEM, X‐ray photoelectron spectroscopy (XPS), Raman, EPR, and N2 sorption measurements. The Pt/La‐TiO2 composite starts to catalyze the CO2 conversion reaction at 220 °C, which is 30 °C lower than the Pt/TiO2 catalyst. The generation of CH4 a… Show more
“…The desorption peak of 0.1% NiO/TiO2 catalyst was more considerable than that of TiO2 (P25), and the desorption temperature was increased by 15°C at the same time. This enhancement is contributed by the surface NiO, which increases the binding between CO2 and the catalyst and benefits to CO2 hydrogenation 50 . Another peak centered at 475°C also belonged to b-CO32−, which might due to the interaction of CO2 and TiO2 on the surface of the catalyst.…”
Section: Resultsmentioning
confidence: 96%
“…This enhancement is contributed by the surface NiO, which increases the binding between CO 2 and the catalyst and benefits to CO 2 hydrogenation. 50 Another peak centered at 475°C also belonged to b-CO 3 2− , which might due to the interaction of CO 2 and TiO 2 on the surface of the catalyst.…”
“…The desorption peak of 0.1% NiO/TiO2 catalyst was more considerable than that of TiO2 (P25), and the desorption temperature was increased by 15°C at the same time. This enhancement is contributed by the surface NiO, which increases the binding between CO2 and the catalyst and benefits to CO2 hydrogenation 50 . Another peak centered at 475°C also belonged to b-CO32−, which might due to the interaction of CO2 and TiO2 on the surface of the catalyst.…”
Section: Resultsmentioning
confidence: 96%
“…This enhancement is contributed by the surface NiO, which increases the binding between CO 2 and the catalyst and benefits to CO 2 hydrogenation. 50 Another peak centered at 475°C also belonged to b-CO 3 2− , which might due to the interaction of CO 2 and TiO 2 on the surface of the catalyst.…”
“…, Ce, La, Y, Eu, Gd, and Er), group 3A metals ( e.g. , Al, In, and Ga), 83,127–132 and transition metals ( e.g. , Cu, Zn, Ni, Fe, and Co) 91,133–138 has been found to be active for the conversion of CO 2 toward different products.…”
Section: Design Of Advanced Nanocatalysts For Thermocatalytic Co2 Con...mentioning
Solid siliceous (silica/silicate) materials remain a handy tool in assisting the defossilization efforts under the aegis of carbon capture and utilization (CCU) for extracting chemicals from “air” rather than “ground”....
“…Interestingly, our previous study found that Al 2 O 3 catalysts alone can offer 100% conversion of COS with better stability where it can withhold the conversion of 50% up to 7 h Adding transition metals, such as Ni, Au, Pd, and Pt, is expected to enhance the catalytic performance since these metals normally facilitate hydrogenation − and C–S bond breaking. − In particular, Pt has been recognized as one of the most efficient catalysts for selective hydrogenation, − , CO oxidation, and C–S bond activation . Such properties could hasten kinetics of COS hydrolysis.…”
Catalytic hydrolysis is considered an effective strategy for treating carbonyl sulfide (COS)�a toxic sulfurcontaining gas that causes problems to the environment and petrochemical industries. Al 2 O 3 -based materials are commonly used as catalysts for COS hydrolysis owing to their stability and cost effectiveness. However, they still suffer from sulfur poisoning leading to partial COS conversion after long time use. To improve their catalytic performances, herein, we computationally designed and studied the catalytic activity of the Pt-supported Al 2 O 3 catalysts by means of density functional calculations. We mechanistically explored the COS hydrolysis on both bare and Pt-decorated surfaces to reveal the role of Pt catalysts in the reaction kinetics. We find that bare Al 2 O 3 suffers from difficult C− S bond breaking as its barrier is relatively high. Pt facilitates C−S bond breaking where its barrier is reduced by more than half (1.34 to 0.60 eV). However, the Pt−Al 2 O 3 catalyst could encounter sulfur poisoning as the sulfur-containing intermediates are rather stable. Such issues could be remedied by increasing the operating temperature to destabilize the intermediates and promote product desorption. The energetic span models reveal that the important states of bare and Pt−Al 2 O 3 are indeed C−S bond breaking and product desorption corresponding to an energy span of 2.72 and 1.67 eV at 773 K, respectively�suggesting that Pt dramatically enhances the catalytic activity of Al 2 O 3 -based catalysts toward COS hydrolysis. The suggested operating temperatures are above 673 K to avoid sulfur poisoning. Our findings will be useful for the development of more efficient Al 2 O 3 -based catalysts for treating COS.
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