dc.contributor
Pérez-Ramírez, Javier
dc.contributor.author
Lari, Giacomo M.
dc.contributor.author
Gröninger, Olivier G.
dc.contributor.author
Li, Qiang
dc.contributor.author
Mondelli, Cecilia
dc.contributor.author
López, Núria
dc.date.accessioned
2019-07-15T14:30:42Z
dc.date.accessioned
2024-04-23T10:16:56Z
dc.date.available
2019-07-15T14:30:42Z
dc.date.available
2024-04-23T10:16:56Z
dc.date.issued
2016-12-20
dc.identifier.uri
http://hdl.handle.net/2072/358877
dc.description.abstract
Sugar alcohols are applied in the food, pharmaceutical, poly- mer, and fuel industries and are commonly obtained by reduc- tion of the corresponding saccharides. In view of the rarity of some sugar substrates, epimerization of a readily available monosaccharide has been proposed as a solution, but an effi- cient catalytic system has not yet been identified. Herein, a mo- lybdenum heteropolyacid-based catalyst is developed to trans- form glucose, arabinose, and xylose into less-abundant man- nose, ribose, and lyxose, respectively. Adsorption of molybdic acid onto activated carbon followed by ion exchange to the cesium form limits leaching of the active phase, which greatly improves the catalyst stability over 24 h on stream. The hydro- genation of mixtures of epimers is studied over ruthenium cat-
alysts, and it is found that the precursor to the desired polyol is advantageously converted with faster kinetics. This is ex- plained by density functional theory on the basis of its more favorable adsorption on the metal surface and the lower energy barrier for the addition of a hydrogen atom to the pri- mary carbon atom. Finally, different designs for a continuous process for the conversion of glucose into mannitol are stud- ied, and it is uncovered that two reactors in series with one containing the epimerization catalyst and the other containing a mixture of the epimerization and hydrogenation catalysts in- creases the mannitol/sorbitol ratio to 1.5 from 1 for a single mixed-bed reactor. This opens a prospective route to the effi- cient valorization of renewables to added-value chemicals.
dc.format.extent
3407 p.
cat
dc.rights
L'accés als continguts d'aquest document queda condicionat a l'acceptació de les condicions d'ús establertes per la següent llicència Creative Commons:http://creativecommons.org/licenses/by-nc-nd/4.0/
dc.source
RECERCAT (Dipòsit de la Recerca de Catalunya)
dc.title
Catalyst and Process Design for the Continuous Manufacture of Rare Sugar Alcohols by Epimerization– Hydrogenation of Aldoses
cat
dc.type
info:eu-repo/semantics/article
cat
dc.type
info:eu-repo/semantics/acceptedVersion
cat
dc.embargo.terms
12 mesos
cat
dc.identifier.doi
https://doi.org/10.1002/cssc.201600755
dc.rights.accessLevel
info:eu-repo/semantics/openAccess