Yomaira Pagan Torres

Dr. Yomaira Pagan Torres

orcid

Research Focus & Metrics

Academic Career Length

21Years (2006-Present)

(Calculated once Scilit publication data is synced: current year − year of first publication + 1)

Representative Publications

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18 April 2012 in ACS Catalysis
Verified
Journal Article
Closed access
YTYomaira Pagan Torres
Yomaira Pagan Torres
TWTianfu Wang
Tianfu Wang
Jean Marcel R GalloJean Marcel R Gallo
Jean Marcel R Gallo
BSBrent H. Shanks
Brent H. Shanks
JDJames A. Dumesic
James A. Dumesic

7 July 2011 in Journal of the American Chemical Society
Verified
Journal Article
Closed access
MCMei Chia
Mei Chia
YTYomaira Pagan Torres
Yomaira Pagan Torres
DHDavid Hibbitts
David Hibbitts
QTQiaohua Tan
Qiaohua Tan
HPHien N. Pham
Hien N. Pham
JDJames A. Dumesic
James A. Dumesic

24 February 2012 in Green Chemistry
Verified
Journal Article
Closed access
PDF file
RARicardo Alamillo
Ricardo Alamillo
MTMark Tucker
Mark Tucker
MCMei Chia
Mei Chia
YTYomaira Pagan Torres
Yomaira Pagan Torres
JDJames Dumesic
James Dumesic
The products produced by hydrogenation of biomass-derived 5-hydroxymethylfurfural (HMF) are potential sustainable substitutes for petroleum-based building blocks used in the production of chemicals. We have studied the hydrogenation of HMF over supported Ru, Pd, and Pt catalysts in monophasic and biphasic reactor systems to determine the effects of the metal, support, solution phase acidity, and the solvent to elucidate the factors that determine the selectivity for hydrogenation of HMF to its fully hydrogenated form of 2,5-di-hydroxy-methyl-tetrahydrofuran (DHMTHF). We show that the selectivity to DHMTHF is affected by the acidity of the aqueous solution containing HMF. The major by-products observed are C6-polyols formed from the acid-catalyzed degradation and subsequent hydrogenation of 2,5-dihydroxymethylfuran (DHMF), an intermediate hydrogenation product of HMF to DHMTHF. The highest yields (88–91%) to DHMTHF are achieved using Ru supported on materials with high isoelectric points, such as ceria, magnesia–zirconia, and γ-alumina. Supported catalysts containing Pt and Pd at the same weight percent as Ru are not as active for the selective hydrogenation to DHMTHF.

14 March 2006 in Molecular Pharmaceutics
Verified
Journal Article
Closed access
NRNaír Rodríguez-Hornedo
Naír Rodríguez-Hornedo
SNSarah J. Nehm
Sarah J. Nehm
KSKurt F. Seefeldt
Kurt F. Seefeldt
YTYomaira Pagan Torres
Yomaira Pagan Torres
CFChristopher J. Falkiewicz
Christopher J. Falkiewicz

1 May 2017 in Catalysis Today
Verified
Journal Article
Closed access
BWBingwen Wang
Bingwen Wang
SASandra Albarracín-Suazo
Sandra Albarracín-Suazo
YTYomaira Pagan Torres
Yomaira Pagan Torres
ENEranda Nikolla
Eranda Nikolla

13 January 2012 in Green Chemistry
Verified
Journal Article
Closed access
PDF file
MHMartin S. Holm
Martin S. Holm
YTYomaira Pagan Torres
Yomaira Pagan Torres
SSShunmugavel Saravanamurugan
Shunmugavel Saravanamurugan
Anders RiisagerAnders Riisager
Anders Riisager
JDJames A. Dumesic
James A. Dumesic
ETEsben Taarning
Esben Taarning
Conversions of various pentoses and hexoses into methyl lactate has been demonstrated for the Sn-Beta catalyst. It is found that pentoses are converted to methyl lactate in slightly lower yields (∼40%) than what is obtained for hexoses (∼50%), but higher yields of glycolaldehyde dimethyl acetal are observed for the pentoses. This finding is in accordance to a reaction pathway that involves the retro aldol condensation of the sugars to form a triose and glycolaldehyde for the pentoses, and two trioses for hexoses. When reacting glycolaldehyde (formally a C2-sugar) in the presence of Sn-Beta, aldol condensation occurs, leading to the formation of methyl lactate, methyl vinylglycolate and methyl 2-hydroxy-4-methoxybutanoate. In contrast, when converting the sugars in water at low temperatures (100 °C), Sn-Beta catalyses the isomerisation of sugars (ketose–aldose epimers), rather than the formation of lactates.