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Conversion of Levulinic Acid Derived Valeric Acid into a Liquid Transportation Fuel of the Kerosene Type Full article

Journal Journal of Molecular Catalysis A: Chemical
ISSN: 1381-1169
Output data Year: 2014, Volume: 388-389, Pages: 116-122 Pages count : 9 DOI: 10.1016/j.molcata.2013.11.015
Tags Catalyst stability, Ketone hydrodeoxygenation, Ketonic decarboxylation, Pt/alumina, Zirconium oxide
Authors Corma Avelino 1 , Oliver-Tomas Borja 1 , Renz Michael 1 , Simakova Irina L. 2
Affiliations
1 Instituto de Tecnología Química, Universitat Politècnica de Valencia-Consejo Superior de Investigaciones Científicas (UPV - CSIC), Av. de los Naranjos s/n, Valencia E-46022, Spain
2 Boreskov Institute of Catalysis, Lavrentieva 5, Novosibirsk 630090, Russian Federation

Funding (3)

1 Spanish National Research Council Es 2010RU0108
2 Ministry of Economic Affairs and Digital Transformation CSD2009-00050
3 Ministry of Economic Affairs and Digital Transformation CTQ2011-27550

Abstract: In the transformation of lignocellulosic biomass into fuels and chemicals carbonsingle bondcarbon bond formations and rising hydrophobicity are highly desired. The ketonic decarboxylation fits these requirements perfectly as it converts carboxylic acids into ketones forming one carbonsingle bondcarbon bond and eliminates three oxygen atoms as carbon dioxide and water. This reaction is used, in a cascade process, together with a hydrogenation and dehydration catalyst to obtain hydrocarbons in the kerosene range from hexose-derived valeric acid. It is shown that zirconium oxide is a very selective and stable catalyst for this process and when combined with platinum supported on alumina, the oxygen content was reduced to almost zero. Furthermore, it is demonstrated that alumina is superior to active carbon, silica, or zirconium oxide as support for the hydrogenation/dehydration/hydrogenation sequence and a palladium-based catalyst deactivated more rapidly than the platinum catalyst. Hence, under optimized reaction conditions valeric acid is converted into n-nonane with 80% selectivity (together with a 10% of C10–C15 hydrocarbons) in the organic liquid phase upto a 100:1 feed to catalyst ratio [w/w]. The oxygen free hydrocarbon product mixture (85% yield) meets well with the boiling point range of kerosene as evidenced by a simulated distillation. In the gas phase, butane was detected together with mainly carbon dioxide.
Cite: Corma A. , Oliver-Tomas B. , Renz M. , Simakova I.L.
Conversion of Levulinic Acid Derived Valeric Acid into a Liquid Transportation Fuel of the Kerosene Type
Journal of Molecular Catalysis A: Chemical. 2014. V.388-389. P.116-122. DOI: 10.1016/j.molcata.2013.11.015 WOS Scopus РИНЦ ANCAN OpenAlex
Files: Full text from publisher
Dates:
Submitted: Jul 26, 2013
Accepted: Nov 11, 2013
Published online: Nov 19, 2013
Published print: Jul 1, 2014
Identifiers:
Web of science: WOS:000337551800013
Scopus: 2-s2.0-84901060237
Elibrary: 21880322
Chemical Abstracts: 2013:1976526
Chemical Abstracts (print): 161:42653
OpenAlex: W1966315427
Citing:
DB Citing
Web of science 27
Scopus 26
Elibrary 29
OpenAlex 29
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