Abstract
The present paper describes the problems arising in studying the kinetics of hydrogenation performed in slurry reactors and the ways to solve them. Two examples are considered: the hydrogenation of 2-ethyltetrahydroanthraquinone, an important step of the industrial production of hydrogen peroxide, and the partial hydrogenation of a rapeseed oil. Both hydrogenations were performed on the same palladium-supported catalyst.
Talk to us
Join us for a 30 min session where you can share your feedback and ask us any queries you have
Disclaimer: All third-party content on this website/platform is and will remain the property of their respective owners and is provided on "as is" basis without any warranties, express or implied. Use of third-party content does not indicate any affiliation, sponsorship with or endorsement by them. Any references to third-party content is to identify the corresponding services and shall be considered fair use under The CopyrightLaw.