Structure-Activity Relationships of Pt-WOx/Al2O3 Prepared with Different W Contents and Pretreatment Conditions for Glycerol Conversion to 1,3-Propanediol

Turning waste glycerol into a fundamental chemical used in the petrochemical industry offers an opportunity to reduce not only waste from biodiesel production but also the consumption of petroleum-based chemicals. In the present work, glycerol was converted to 1,3-propanediol over Pt-WO x /Al 2 O 3...

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Bibliographic Details
Published inTopics in catalysis Vol. 66; no. 1-4; pp. 205 - 222
Main Authors Dolsiririttigul, Napaphut, Numpilai, Thanapha, Wattanakit, Chularat, Seubsai, Anusorn, Faungnawakij, Kajornsak, Cheng, Chin Kui, Vo, Dai-Viet N., Nijpanich, Supinya, Chanlek, Narong, Witoon, Thongthai
Format Journal Article
LanguageEnglish
Published New York Springer US 2023
Springer Nature B.V
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Summary:Turning waste glycerol into a fundamental chemical used in the petrochemical industry offers an opportunity to reduce not only waste from biodiesel production but also the consumption of petroleum-based chemicals. In the present work, glycerol was converted to 1,3-propanediol over Pt-WO x /Al 2 O 3 catalysts, while focusing on the influence of W loading contents (10–20 wt.%) and catalyst pretreatment conditions, specifically the calcination temperatures of WO x /Al 2 O 3 (700–900 °C), calcination temperatures of Pt-WO x /Al 2 O 3 (350–450 °C) and reduction temperatures of Pt-WO x /Al 2 O 3 (300–400 °C). The characteristics of the catalysts were identified by applying N 2 -sorption, XRD, Raman, CO pulse chemisorption, NH 3 -TPD, H 2 -TPR, H 2 -TPD, SEM and TEM-EDS and XPS. The W loading contents and pretreatment conditions strongly affected the activity and products selectivity. The W content and calcination temperature of WO x /Al 2 O 3 at 15 wt.% and 800 °C, respectively, were evaluated as the most suitable in providing optimum W-O-W clusters to generate H δ+ which was a key parameter for the generation of 1,3-propanediol. The calcination and reduction temperatures of Pt-WO x /Al 2 O 3 at 400 °C and 350 °C, respectively, were mandatory to sufficiently convert PtCl 2 to Pt 3 O 4 and Pt 3 O 4 to metallic Pt, respectively. The optimized Pt-WO x /Al 2 O 3 catalyst achieved a high glycerol conversion (44.7%) with high selectivity toward 1,3-propanediol (45.1%) under a reaction temperature and pressure of 220 °C and 60 bar, respectively.
ISSN:1022-5528
1572-9028
DOI:10.1007/s11244-022-01753-9