Abstract
Pyrolysis bio-oils contain significant amounts of carboxylic acids which limit their utility as biofuels. Ketonisation of carboxylic acids within biomass pyrolysis vapours is a potential route to upgrade the energy content and stability of the resulting bio-oil condensate, but requires active, selective and coke-resistant solid acid catalysts. Here we explore the vapour phase ketonisation of acetic acid over Ga-doped HZSM-5. Weak Lewis acid sites were identified as the active species responsible for acetic acid ketonisation to acetone at 350 ◦C and 400 ◦C. Turnover frequencies were proportional to Ga loading, reaching ~6 min −1 at 400 ◦C for 10Ga/HZSM-5. Selectivity to the desired acetone product correlated with the weak:strong acid site ratio, being favoured over weak Lewis acid sites and reaching 30% for 10Ga/HZSM-5. Strong Brønsted acidity promoted competing unselective reactions and carbon laydown. 10Ga/HZSM-5 exhibited good stability for over 5 h on-stream acetic acid ketonisation.
Original language | English |
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Article number | 841 |
Journal | Catalysts |
Volume | 9 |
Issue number | 10 |
DOIs | |
Publication status | Published - 11 Oct 2019 |
Bibliographical note
© 2019 by the authors. Licensee MDPI, Basel, Switzerland. This article is an open access article distributed under the terms and conditions of the Creative Commons Attribution (CC BY) license (http://creativecommons.org/licenses/by/4.0/).Funding: EPSRC (EP/K036548/2, EP/K014676/1, EP/N009924/1), the Royal Society Industry Fellowship.
Keywords
- Bio-oil
- Ketonisation
- Pyrolysis
- Turnover frequencies (TOFs)