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Aldol-condensation of furfural by activated dolomite catalyst

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Aldol-condensation of furfural by activated dolomite catalyst. / O’Neill, Rebecca ; Vanoye, Laurent; De Bellefon, Claude et al.
In: Applied Catalysis B: Environmental, Vol. 144, 01.2014, p. 46-56.

Research output: Contribution to Journal/MagazineJournal articlepeer-review

Harvard

O’Neill, R, Vanoye, L, De Bellefon, C & Aiouache, F 2014, 'Aldol-condensation of furfural by activated dolomite catalyst', Applied Catalysis B: Environmental, vol. 144, pp. 46-56. https://doi.org/10.1016/j.apcatb.2013.07.006

APA

O’Neill, R., Vanoye, L., De Bellefon, C., & Aiouache, F. (2014). Aldol-condensation of furfural by activated dolomite catalyst. Applied Catalysis B: Environmental, 144, 46-56. https://doi.org/10.1016/j.apcatb.2013.07.006

Vancouver

O’Neill R, Vanoye L, De Bellefon C, Aiouache F. Aldol-condensation of furfural by activated dolomite catalyst. Applied Catalysis B: Environmental. 2014 Jan;144:46-56. doi: 10.1016/j.apcatb.2013.07.006

Author

O’Neill, Rebecca ; Vanoye, Laurent ; De Bellefon, Claude et al. / Aldol-condensation of furfural by activated dolomite catalyst. In: Applied Catalysis B: Environmental. 2014 ; Vol. 144. pp. 46-56.

Bibtex

@article{e1dd41a6d67248eaa6013123ef80794e,
title = "Aldol-condensation of furfural by activated dolomite catalyst",
abstract = "Aldol-condensation of furfural with acetone catalysed by activated dolomite was investigated at temperatures from 306 to 413 K. The process of activation by calcination and hydration produced catalytically active calcium and magnesium hydroxides with improved surface area and surface basicity. The aldol-condensation mechanism began with a deprotonation of acetone forming a carbanion intermediate by hydroxyl ions, which then reacted with the carbonyl group of furfural to form a water soluble C8 monomer (4-(furan-2-yl)-4-hydroxybutan-2-one). This C8 monomer readily dehydrated to form selectively α,β-unsaturated ketone (4-(2-furyl)-3-buten-2-one), which in turn, reacted with furfural forming a C13 dimer (1,4-pentadien-3-one,1,5-di-2-furanyl). Compared with conventional sodium hydroxide catalyst, activated dolomite was less selective towards lumped C8 monomers and C13 dimers owing to carbon losses and deactivation, particularly at high temperatures. Activated dolomite was more selective to C13 dimer owing to higher adsorption enthalpy of C8 monomer compared with acetone competitor. Activated dolomite is therefore a promising catalyst to produce C13 dimers which can be transformed upon hydrogenation and deep hydrodeoxygenation in high-quality diesel fuels. The first-order kinetic model with respect to furfural and acetone fitted well with actual experimental results with an average normalised standard deviation of 6.2%.",
keywords = "basic catalysis, aldol condensation, kinetics and mechanisms, doomite, mixe oxide catalysist",
author = "Rebecca O{\textquoteright}Neill and Laurent Vanoye and {De Bellefon}, Claude and Farid Aiouache",
year = "2014",
month = jan,
doi = "10.1016/j.apcatb.2013.07.006",
language = "English",
volume = "144",
pages = "46--56",
journal = "Applied Catalysis B: Environmental",
issn = "0926-3373",
publisher = "Elsevier",

}

RIS

TY - JOUR

T1 - Aldol-condensation of furfural by activated dolomite catalyst

AU - O’Neill, Rebecca

AU - Vanoye, Laurent

AU - De Bellefon, Claude

AU - Aiouache, Farid

PY - 2014/1

Y1 - 2014/1

N2 - Aldol-condensation of furfural with acetone catalysed by activated dolomite was investigated at temperatures from 306 to 413 K. The process of activation by calcination and hydration produced catalytically active calcium and magnesium hydroxides with improved surface area and surface basicity. The aldol-condensation mechanism began with a deprotonation of acetone forming a carbanion intermediate by hydroxyl ions, which then reacted with the carbonyl group of furfural to form a water soluble C8 monomer (4-(furan-2-yl)-4-hydroxybutan-2-one). This C8 monomer readily dehydrated to form selectively α,β-unsaturated ketone (4-(2-furyl)-3-buten-2-one), which in turn, reacted with furfural forming a C13 dimer (1,4-pentadien-3-one,1,5-di-2-furanyl). Compared with conventional sodium hydroxide catalyst, activated dolomite was less selective towards lumped C8 monomers and C13 dimers owing to carbon losses and deactivation, particularly at high temperatures. Activated dolomite was more selective to C13 dimer owing to higher adsorption enthalpy of C8 monomer compared with acetone competitor. Activated dolomite is therefore a promising catalyst to produce C13 dimers which can be transformed upon hydrogenation and deep hydrodeoxygenation in high-quality diesel fuels. The first-order kinetic model with respect to furfural and acetone fitted well with actual experimental results with an average normalised standard deviation of 6.2%.

AB - Aldol-condensation of furfural with acetone catalysed by activated dolomite was investigated at temperatures from 306 to 413 K. The process of activation by calcination and hydration produced catalytically active calcium and magnesium hydroxides with improved surface area and surface basicity. The aldol-condensation mechanism began with a deprotonation of acetone forming a carbanion intermediate by hydroxyl ions, which then reacted with the carbonyl group of furfural to form a water soluble C8 monomer (4-(furan-2-yl)-4-hydroxybutan-2-one). This C8 monomer readily dehydrated to form selectively α,β-unsaturated ketone (4-(2-furyl)-3-buten-2-one), which in turn, reacted with furfural forming a C13 dimer (1,4-pentadien-3-one,1,5-di-2-furanyl). Compared with conventional sodium hydroxide catalyst, activated dolomite was less selective towards lumped C8 monomers and C13 dimers owing to carbon losses and deactivation, particularly at high temperatures. Activated dolomite was more selective to C13 dimer owing to higher adsorption enthalpy of C8 monomer compared with acetone competitor. Activated dolomite is therefore a promising catalyst to produce C13 dimers which can be transformed upon hydrogenation and deep hydrodeoxygenation in high-quality diesel fuels. The first-order kinetic model with respect to furfural and acetone fitted well with actual experimental results with an average normalised standard deviation of 6.2%.

KW - basic catalysis

KW - aldol condensation

KW - kinetics and mechanisms

KW - doomite

KW - mixe oxide catalysist

U2 - 10.1016/j.apcatb.2013.07.006

DO - 10.1016/j.apcatb.2013.07.006

M3 - Journal article

VL - 144

SP - 46

EP - 56

JO - Applied Catalysis B: Environmental

JF - Applied Catalysis B: Environmental

SN - 0926-3373

ER -