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- Publisher Website: 10.1021/ef500147k
- Scopus: eid_2-s2.0-84900555381
- WOS: WOS:000336199300055
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Article: Hydrogenolysis of Glycerol by the Combined Use of Zeolite and Ni/A2O3 as Catalysts: A Route for Achieving High Selectivity to 1-Propanol
Title | Hydrogenolysis of Glycerol by the Combined Use of Zeolite and Ni/A2O3 as Catalysts: A Route for Achieving High Selectivity to 1-Propanol |
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Authors | |
Issue Date | 2014 |
Citation | Energy & Fuels, 2014, v. 28, p. 3345-3351 How to Cite? |
Abstract | Sequential two-layer catalysts were used for the hydrogenolysis of glycerol to remove its oxygen content in a continuous-flow fixed-bed reactor. The acidic H-β catalyst layer was packed before the Ni/Al2O3 catalyst layer in the reactor. The sequential two-layer catalysts can provide good 1-propanol (1-PO) selectivities at high glycerol conversions (up to 69% selectivity at 100% conversion). To our knowledge, the catalytic system in this work presented one of the best selectivities to 1-PO using non-noble metal based catalytic systems. A preliminary mechanistic study indicated that most of 1-PO in the products was generated from glycerol via a “sequential two-time dehydration-hydrogenation” mechanism. |
Persistent Identifier | http://hdl.handle.net/10722/202574 |
ISSN | 2023 Impact Factor: 5.2 2023 SCImago Journal Rankings: 1.018 |
ISI Accession Number ID |
DC Field | Value | Language |
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dc.contributor.author | Lin, X | en_US |
dc.contributor.author | Lv, Y | en_US |
dc.contributor.author | Xi, Y | en_US |
dc.contributor.author | Qu, Y | en_US |
dc.contributor.author | Phillips, DL | en_US |
dc.contributor.author | Liu, C | en_US |
dc.date.accessioned | 2014-09-19T08:41:24Z | - |
dc.date.available | 2014-09-19T08:41:24Z | - |
dc.date.issued | 2014 | en_US |
dc.identifier.citation | Energy & Fuels, 2014, v. 28, p. 3345-3351 | en_US |
dc.identifier.issn | 0887-0624 | - |
dc.identifier.uri | http://hdl.handle.net/10722/202574 | - |
dc.description.abstract | Sequential two-layer catalysts were used for the hydrogenolysis of glycerol to remove its oxygen content in a continuous-flow fixed-bed reactor. The acidic H-β catalyst layer was packed before the Ni/Al2O3 catalyst layer in the reactor. The sequential two-layer catalysts can provide good 1-propanol (1-PO) selectivities at high glycerol conversions (up to 69% selectivity at 100% conversion). To our knowledge, the catalytic system in this work presented one of the best selectivities to 1-PO using non-noble metal based catalytic systems. A preliminary mechanistic study indicated that most of 1-PO in the products was generated from glycerol via a “sequential two-time dehydration-hydrogenation” mechanism. | en_US |
dc.language | eng | en_US |
dc.relation.ispartof | Energy & Fuels | en_US |
dc.title | Hydrogenolysis of Glycerol by the Combined Use of Zeolite and Ni/A2O3 as Catalysts: A Route for Achieving High Selectivity to 1-Propanol | en_US |
dc.type | Article | en_US |
dc.identifier.email | Phillips, DL: phillips@hku.hk | en_US |
dc.identifier.authority | Phillips, DL=rp00770 | en_US |
dc.identifier.doi | 10.1021/ef500147k | en_US |
dc.identifier.scopus | eid_2-s2.0-84900555381 | - |
dc.identifier.hkuros | 237041 | en_US |
dc.identifier.volume | 28 | en_US |
dc.identifier.spage | 3345 | en_US |
dc.identifier.epage | 3351 | en_US |
dc.identifier.eissn | 1520-5029 | - |
dc.identifier.isi | WOS:000336199300055 | - |
dc.identifier.issnl | 0887-0624 | - |