Abstract

The deoxygenation of palmitic acid into diesel-range hydrocarbons can be promoted over nanocrystalline ceria-based catalysts under atmospheric N2 or 10% H2/N2 in a fixed-bed flow reactor at 400°C. Oxygen vacancy sites are active for ketonization of palmitic acid to C31 ketone and also subsequent cracking of the formed ketone to hydrocarbons. The 22–31% selectivity of C9 to C17 liquid hydrocarbons can be achieved at 100% palmitic acid conversion. The deoxygenation under N2 can be facilitated, presumably by hydrogen transfer from coke precursors. Catalytic activity of ceria-based catalysts can be tuned by pretreatment conditions, type of a carrier gas, or lattice modification.

Full Text
Paper version not known

Talk to us

Join us for a 30 min session where you can share your feedback and ask us any queries you have

Schedule a call

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.