Catalytic activity of tungsten-doped titanium dioxide-supported platinum catalysts in the sequential hydrogenolysis of glycerol: effect of support calcination temperature
{"title":"Catalytic activity of tungsten-doped titanium dioxide-supported platinum catalysts in the sequential hydrogenolysis of glycerol: effect of support calcination temperature","authors":"Chao Yu, Changlin Chen","doi":"10.1007/s11144-025-02822-2","DOIUrl":null,"url":null,"abstract":"<div><p>Two Pt-WO<sub>x</sub>/TiO<sub>2</sub> catalysts with the same content of Pt and WO<sub>x</sub> were prepared by impregnation-calcination method and treated with WO<sub>x</sub>/TiO<sub>2</sub> supports at different temperatures, and their catalytic performance in the preparation of 1,3-propanediol (1,3-PDO) by selective hydrogenolysis of glycerol was studied. The catalysts were characterized by N<sub>2</sub> adsorption–desorption, CO chemisorption, Thermogravimetric analysis, X-ray diffraction, High-resolution transmission electron microscopy, NH<sub>3</sub>-temperature-programmed desorption, H<sub>2</sub>-temperature-programmed reduction, Fourier transform infrared spectroscopy and X-ray photoelectron spectroscopy. The results showed that the Pt-WO<sub>x</sub>/TiO<sub>2</sub> catalyst with high temperature treatment had the highest activity, with a glycerol conversion rate of 71.4% and a selectivity of 36.4% for 1,3-PDO at 160 °C and 4 MPa, while the catalyst treated with low temperature was only 5.2% and 10.6%. In this regard, increasing the treatment temperature of the catalyst did not change the crystalline phase structure of TiO<sub>2</sub>, but changed the diameter structure of the catalyst pore, improved the crystallinity of the catalyst support and the dispersion of Pt particles on the surface, reduced the amount of acid in the catalyst, and enhanced the interaction between Pt, WO<sub>x</sub> and TiO<sub>2</sub> in the catalyst.</p></div>","PeriodicalId":750,"journal":{"name":"Reaction Kinetics, Mechanisms and Catalysis","volume":"138 3","pages":"1479 - 1494"},"PeriodicalIF":1.7000,"publicationDate":"2025-02-23","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Reaction Kinetics, Mechanisms and Catalysis","FirstCategoryId":"92","ListUrlMain":"https://link.springer.com/article/10.1007/s11144-025-02822-2","RegionNum":4,"RegionCategory":"化学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q4","JCRName":"CHEMISTRY, PHYSICAL","Score":null,"Total":0}
引用次数: 0
Abstract
Two Pt-WOx/TiO2 catalysts with the same content of Pt and WOx were prepared by impregnation-calcination method and treated with WOx/TiO2 supports at different temperatures, and their catalytic performance in the preparation of 1,3-propanediol (1,3-PDO) by selective hydrogenolysis of glycerol was studied. The catalysts were characterized by N2 adsorption–desorption, CO chemisorption, Thermogravimetric analysis, X-ray diffraction, High-resolution transmission electron microscopy, NH3-temperature-programmed desorption, H2-temperature-programmed reduction, Fourier transform infrared spectroscopy and X-ray photoelectron spectroscopy. The results showed that the Pt-WOx/TiO2 catalyst with high temperature treatment had the highest activity, with a glycerol conversion rate of 71.4% and a selectivity of 36.4% for 1,3-PDO at 160 °C and 4 MPa, while the catalyst treated with low temperature was only 5.2% and 10.6%. In this regard, increasing the treatment temperature of the catalyst did not change the crystalline phase structure of TiO2, but changed the diameter structure of the catalyst pore, improved the crystallinity of the catalyst support and the dispersion of Pt particles on the surface, reduced the amount of acid in the catalyst, and enhanced the interaction between Pt, WOx and TiO2 in the catalyst.
期刊介绍:
Reaction Kinetics, Mechanisms and Catalysis is a medium for original contributions in the following fields:
-kinetics of homogeneous reactions in gas, liquid and solid phase;
-Homogeneous catalysis;
-Heterogeneous catalysis;
-Adsorption in heterogeneous catalysis;
-Transport processes related to reaction kinetics and catalysis;
-Preparation and study of catalysts;
-Reactors and apparatus.
Reaction Kinetics, Mechanisms and Catalysis was formerly published under the title Reaction Kinetics and Catalysis Letters.