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Highly efficient TiO2-supported Co–Cu catalysts for conversion of glycerol to 1,2-propanediol
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by นพพร ม่วงระย้า  
Metadata
Document Title
Highly efficient TiO2-supported Co–Cu catalysts for conversion of glycerol to 1,2-propanediol
Author
Mondach W., Chanklang S., Somchuea P., Witoon T., Chareonpanich M., Faungnawakij K., Sohn H., Seubsai A.
Name from Authors Collection
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Affiliations
Department of Chemical Engineering, Faculty of Engineering, Kasetsart University, Bangkok, 10900, Thailand; Center of Excellence on Petrochemical and Materials Technology, Kasetsart University, Bangkok, 10900, Thailand; Research Network of NANOTEC–KU on NanoCatalysts and NanoMaterials for Sustainable Energy and Environment, Kasetsart University, Bangkok, 10900, Thailand; Nanomaterials for Energy and Catalysis Laboratory, National Nanotechnology Center (NANOTEC), National Science and Technology Development Agency (NSTDA), Klong Laung, Pathumthani, 12120, Thailand; Department of Chemical Engineering, Kwangwoon University, Seoul, 01897, South Korea
Type
Article
Source Title
Scientific Reports
ISSN
20452322
Year
2021
Volume
11
Issue
1
Open Access
Gold, Green
Publisher
Nature Research
DOI
10.1038/s41598-021-02416-7
Abstract
Glycerol is a low-cost byproduct of the biodiesel manufacturing process, which can be used to synthesize various value-added chemicals. Among them, 1,2-propanediol (1,2-PDO) is of great interest because it can be used as an intermediate and additive in many applications. This work investigated the hydrogenolysis of glycerol to 1,2-PDO over Co–Cu bimetallic catalysts supported on TiO2 (denoted as CoCu/TiO2) in aqueous media. The catalysts were prepared using the co-impregnation method and their physicochemical properties were characterized using several techniques. The addition of appropriate Cu increased the glycerol conversion and the 1,2-PDO yield. The highest 1,2-PDO yield was achieved over a 15Co0.5Cu/TiO2 catalyst at 69.5% (glycerol conversion of 95.2% and 1,2-PDO selectivity of 73.0%). In the study on the effects of operating conditions, increasing the reaction temperature, initial pressure, and reaction time increased the glycerol conversion but decreased the selectivity to 1,2-PDO due to the degradation of formed 1,2-PDO to lower alcohols (1-propanol and 2-propanol). The reaction conditions to obtain the maximum 1,2-PDO yield were a catalyst-to-glycerol ratio of 0.028, a reaction temperature of 250 °C, an initial H2 pressure of 4 MPa, and a reaction time of 4 h. © 2021, The Author(s).
Funding Sponsor
National Science and Technology Development Agency; Kasetsart University Research and Development Institute; National Nanotechnology Center; Ministry of Science and Technology of Thailand; Center of Excellence on Petrochemical and Materials Technology
License
CC BY
Rights
Author
Publication Source
Scopus