Hydrogen-free catalytic conversion of highly concentrated glycerol solution: Influence of Si/Al molar ratio in Cu/SBA-15 catalysts.
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| Title: | Hydrogen-free catalytic conversion of highly concentrated glycerol solution: Influence of Si/Al molar ratio in Cu/SBA-15 catalysts. |
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| Authors: | Gajardo, Jorge1 (AUTHOR), Colmenares-Zerpa, Julio1,2 (AUTHOR), Peixoto, A.F.3 (AUTHOR), Silva, D.S.A.4 (AUTHOR), Gispert-Guirado, F.5 (AUTHOR), Llorca, J.6 (AUTHOR), Urquieta-Gonzalez, E.A.4,7 (AUTHOR), Santos, J.B.O.4 (AUTHOR), Álvarez, M.G.1,8 (AUTHOR) mgalvarez@usal.es, Chimentão, R.J.1 (AUTHOR) rchimenton@udec.cl |
| Source: | Applied Catalysis A: General. Dec2025, Vol. 708, pN.PAG-N.PAG. 1p. |
| Subjects: | Glycerin, Hydroxypropanone, Catalytic activity, Copper catalysts, Energy development, Catalyst structure, Catalytic hydrogenation |
| Abstract: | Catalytic conversion of glycerol to C 3 products using advanced functional materials is an economical and efficient approach to promoting sustainable energy development. Selective glycerol dehydration to hydroxyacetone (HA) is one such alternative and requires an appropriate balance of catalyst texture, structure, and acidity. In this study, different Cu-based catalysts supported on SBA-15 with different Si/Al molar ratios (2, 10, 15 and ∞) were prepared using the "pH-adjusting" method and ammonia evaporation method and they were evaluated for the dehydration of glycerol at high concentration (80 wt%.) in liquid phase to hydroxyacetone under inert N 2 atmosphere. The formation of 1,2-propanediol (1,2-PDO) was also observed even under N 2 inert atmosphere conditions. The catalysts were characterized by ICP-MS, N 2 adsorption-desorption, XRD, HRTEM, H 2 -TPR, passivation of N 2 O, NH 3 -TPD, TPO, FTIR, FTIR-OH, Py-FTIR and XPS. The Al chemical environment and the Si/Al molar ratio of the supports show a remarkable effect on the catalytic performance. The highest catalytic activity was obtained with the SiAl = 15 molar ratio, reaching a conversion of around 35 % at 120 min of reaction and a selectivity of 84 % to hydroxyacetone at 90 min of reaction. While lower Si/Al molar ratios led to a decrease in catalytic activity and an increase in product distribution. The isomorphic incorporation of Al into the SBA-15 promotes the interlinking cooperative between the properties of textural, acidity, structural, and stability of the catalyst. HRTEM and HAADF-STEM images show a well-defined hexagonal arrangement even when the CuO phase is added to the mesoporous materials with high Al loadings. At high heteroatom loadings, the typical hexagonal arrangement of the mesostructure was preserved but a decrease in the long-range order was observed. The presence of mononuclear and oligonuclear Cuδ+ species, which is related to their coordination environment and their position in the mesoporous network, was dependent on the variation of the Si/Al molar ratio. The prominent catalytic performance at the SiAl = 15 ratio can be attributed to an optimal cooperative effect of the structural defects and electronic promotion produced by the Al species, which favors the conversion of glycerol to HA. While the increase in the selectivity of 1,2-PDO observed with the molar ratio SiAl = 2 is associated with a conjugation between the higher availability of acid sites on the surface that promote the dehydration of glycerol and the domain size of copper species which would be acting as dehydrogenating sites of glycerol, forming H 2 in - situ leading to the conversion of HA into 1,2-PDO. [Display omitted] • Synthesis of Cu/SBA-15 with different Si/Al ratios. • Textural, structural, acid, and surface properties change with the Si/Al ratio. • High concentration glycerol dehydration under an inert atmosphere. • Intra-framework Al species were formed in the Cu/Al-SBA-15 with the lower Al load. • Incorporation of copper by ammonia-evaporation (AE) method. [ABSTRACT FROM AUTHOR] |
| Copyright of Applied Catalysis A: General is the property of Elsevier B.V. and its content may not be copied or emailed to multiple sites without the copyright holder's express written permission. Additionally, content may not be used with any artificial intelligence tools or machine learning technologies. However, users may print, download, or email articles for individual use. This abstract may be abridged. No warranty is given about the accuracy of the copy. Users should refer to the original published version of the material for the full abstract. (Copyright applies to all Abstracts.) | |
| Database: | Engineering Source |
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| Header | DbId: egs DbLabel: Engineering Source An: 188598164 AccessLevel: 6 PubType: Academic Journal PubTypeId: academicJournal PreciseRelevancyScore: 0 |
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| Items | – Name: Title Label: Title Group: Ti Data: Hydrogen-free catalytic conversion of highly concentrated glycerol solution: Influence of Si/Al molar ratio in Cu/SBA-15 catalysts. – Name: Author Label: Authors Group: Au Data: <searchLink fieldCode="AR" term="%22Gajardo%2C+Jorge%22">Gajardo, Jorge</searchLink><relatesTo>1</relatesTo> (AUTHOR)<br /><searchLink fieldCode="AR" term="%22Colmenares-Zerpa%2C+Julio%22">Colmenares-Zerpa, Julio</searchLink><relatesTo>1,2</relatesTo> (AUTHOR)<br /><searchLink fieldCode="AR" term="%22Peixoto%2C+A%2EF%2E%22">Peixoto, A.F.</searchLink><relatesTo>3</relatesTo> (AUTHOR)<br /><searchLink fieldCode="AR" term="%22Silva%2C+D%2ES%2EA%2E%22">Silva, D.S.A.</searchLink><relatesTo>4</relatesTo> (AUTHOR)<br /><searchLink fieldCode="AR" term="%22Gispert-Guirado%2C+F%2E%22">Gispert-Guirado, F.</searchLink><relatesTo>5</relatesTo> (AUTHOR)<br /><searchLink fieldCode="AR" term="%22Llorca%2C+J%2E%22">Llorca, J.</searchLink><relatesTo>6</relatesTo> (AUTHOR)<br /><searchLink fieldCode="AR" term="%22Urquieta-Gonzalez%2C+E%2EA%2E%22">Urquieta-Gonzalez, E.A.</searchLink><relatesTo>4,7</relatesTo> (AUTHOR)<br /><searchLink fieldCode="AR" term="%22Santos%2C+J%2EB%2EO%2E%22">Santos, J.B.O.</searchLink><relatesTo>4</relatesTo> (AUTHOR)<br /><searchLink fieldCode="AR" term="%22Álvarez%2C+M%2EG%2E%22">Álvarez, M.G.</searchLink><relatesTo>1,8</relatesTo> (AUTHOR)<i> mgalvarez@usal.es</i><br /><searchLink fieldCode="AR" term="%22Chimentão%2C+R%2EJ%2E%22">Chimentão, R.J.</searchLink><relatesTo>1</relatesTo> (AUTHOR)<i> rchimenton@udec.cl</i> – Name: TitleSource Label: Source Group: Src Data: <searchLink fieldCode="JN" term="%22Applied+Catalysis+A%3A+General%22">Applied Catalysis A: General</searchLink>. Dec2025, Vol. 708, pN.PAG-N.PAG. 1p. – Name: Subject Label: Subjects Group: Su Data: <searchLink fieldCode="DE" term="%22Glycerin%22">Glycerin</searchLink><br /><searchLink fieldCode="DE" term="%22Hydroxypropanone%22">Hydroxypropanone</searchLink><br /><searchLink fieldCode="DE" term="%22Catalytic+activity%22">Catalytic activity</searchLink><br /><searchLink fieldCode="DE" term="%22Copper+catalysts%22">Copper catalysts</searchLink><br /><searchLink fieldCode="DE" term="%22Energy+development%22">Energy development</searchLink><br /><searchLink fieldCode="DE" term="%22Catalyst+structure%22">Catalyst structure</searchLink><br /><searchLink fieldCode="DE" term="%22Catalytic+hydrogenation%22">Catalytic hydrogenation</searchLink> – Name: Abstract Label: Abstract Group: Ab Data: Catalytic conversion of glycerol to C 3 products using advanced functional materials is an economical and efficient approach to promoting sustainable energy development. Selective glycerol dehydration to hydroxyacetone (HA) is one such alternative and requires an appropriate balance of catalyst texture, structure, and acidity. In this study, different Cu-based catalysts supported on SBA-15 with different Si/Al molar ratios (2, 10, 15 and ∞) were prepared using the "pH-adjusting" method and ammonia evaporation method and they were evaluated for the dehydration of glycerol at high concentration (80 wt%.) in liquid phase to hydroxyacetone under inert N 2 atmosphere. The formation of 1,2-propanediol (1,2-PDO) was also observed even under N 2 inert atmosphere conditions. The catalysts were characterized by ICP-MS, N 2 adsorption-desorption, XRD, HRTEM, H 2 -TPR, passivation of N 2 O, NH 3 -TPD, TPO, FTIR, FTIR-OH, Py-FTIR and XPS. The Al chemical environment and the Si/Al molar ratio of the supports show a remarkable effect on the catalytic performance. The highest catalytic activity was obtained with the SiAl = 15 molar ratio, reaching a conversion of around 35 % at 120 min of reaction and a selectivity of 84 % to hydroxyacetone at 90 min of reaction. While lower Si/Al molar ratios led to a decrease in catalytic activity and an increase in product distribution. The isomorphic incorporation of Al into the SBA-15 promotes the interlinking cooperative between the properties of textural, acidity, structural, and stability of the catalyst. HRTEM and HAADF-STEM images show a well-defined hexagonal arrangement even when the CuO phase is added to the mesoporous materials with high Al loadings. At high heteroatom loadings, the typical hexagonal arrangement of the mesostructure was preserved but a decrease in the long-range order was observed. The presence of mononuclear and oligonuclear Cuδ+ species, which is related to their coordination environment and their position in the mesoporous network, was dependent on the variation of the Si/Al molar ratio. The prominent catalytic performance at the SiAl = 15 ratio can be attributed to an optimal cooperative effect of the structural defects and electronic promotion produced by the Al species, which favors the conversion of glycerol to HA. While the increase in the selectivity of 1,2-PDO observed with the molar ratio SiAl = 2 is associated with a conjugation between the higher availability of acid sites on the surface that promote the dehydration of glycerol and the domain size of copper species which would be acting as dehydrogenating sites of glycerol, forming H 2 in - situ leading to the conversion of HA into 1,2-PDO. [Display omitted] • Synthesis of Cu/SBA-15 with different Si/Al ratios. • Textural, structural, acid, and surface properties change with the Si/Al ratio. • High concentration glycerol dehydration under an inert atmosphere. • Intra-framework Al species were formed in the Cu/Al-SBA-15 with the lower Al load. • Incorporation of copper by ammonia-evaporation (AE) method. [ABSTRACT FROM AUTHOR] – Name: AbstractSuppliedCopyright Label: Group: Ab Data: <i>Copyright of Applied Catalysis A: General is the property of Elsevier B.V. and its content may not be copied or emailed to multiple sites without the copyright holder's express written permission. Additionally, content may not be used with any artificial intelligence tools or machine learning technologies. However, users may print, download, or email articles for individual use. This abstract may be abridged. No warranty is given about the accuracy of the copy. Users should refer to the original published version of the material for the full abstract.</i> (Copyright applies to all Abstracts.) |
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| RecordInfo | BibRecord: BibEntity: Identifiers: – Type: doi Value: 10.1016/j.apcata.2025.120528 Languages: – Code: eng Text: English PhysicalDescription: Pagination: PageCount: 1 StartPage: N.PAG Subjects: – SubjectFull: Glycerin Type: general – SubjectFull: Hydroxypropanone Type: general – SubjectFull: Catalytic activity Type: general – SubjectFull: Copper catalysts Type: general – SubjectFull: Energy development Type: general – SubjectFull: Catalyst structure Type: general – SubjectFull: Catalytic hydrogenation Type: general Titles: – TitleFull: Hydrogen-free catalytic conversion of highly concentrated glycerol solution: Influence of Si/Al molar ratio in Cu/SBA-15 catalysts. Type: main BibRelationships: HasContributorRelationships: – PersonEntity: Name: NameFull: Gajardo, Jorge – PersonEntity: Name: NameFull: Colmenares-Zerpa, Julio – PersonEntity: Name: NameFull: Peixoto, A.F. – PersonEntity: Name: NameFull: Silva, D.S.A. – PersonEntity: Name: NameFull: Gispert-Guirado, F. – PersonEntity: Name: NameFull: Llorca, J. – PersonEntity: Name: NameFull: Urquieta-Gonzalez, E.A. – PersonEntity: Name: NameFull: Santos, J.B.O. – PersonEntity: Name: NameFull: Álvarez, M.G. – PersonEntity: Name: NameFull: Chimentão, R.J. IsPartOfRelationships: – BibEntity: Dates: – D: 25 M: 12 Text: Dec2025 Type: published Y: 2025 Identifiers: – Type: issn-print Value: 0926860X Numbering: – Type: volume Value: 708 Titles: – TitleFull: Applied Catalysis A: General Type: main |
| ResultId | 1 |
