2010
DOI: 10.1007/s11244-010-9576-7
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Aldol Condensations Using Bio-oil Model Compounds: The Role of Acid–Base Bi-functionality

Abstract: The aldol condensation of acetaldehyde, acetone, and methyl ethyl ketone, which represent model biooil compounds, in the condensed phase, was performed using a bi-functional aluminophosphate catalyst. It was found that increasing the number and strength of the basic sites while decreasing acid sites on the catalyst caused a reduction in yield of the condensation products. In contrast, the addition of organic acids such as acetic acid at low concentrations to the catalyst-containing reaction mixture was found t… Show more

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Cited by 35 publications
(31 citation statements)
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“…[47][48][49][50] In the reactionc atalyzed by ZrO 2 /n-ZSM-5-ATP (Figure 3a,b), styrene oligomers were formed, but to a lower extent than over the n-ZSM-5 ( Figure 3c)a nd ZrO 2 /n-ZSM-5 ( Figure 3d)c atalysts. The intensity evolution of the cyclic oligomers (7), favored in zones with high densities of Brønsted acid sites, was particularly low for the ZrO 2 /n-ZSM-5-ATPc atalyst. On the contrary,t he formation of linear dimer (5) was more pronounced, especially in the first 5min of the reaction;a fterwards, the relative amount of trimero ligomers (6a and 6b)i ncreased.…”
Section: Catalyst Propertiesmentioning
confidence: 95%
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“…[47][48][49][50] In the reactionc atalyzed by ZrO 2 /n-ZSM-5-ATP (Figure 3a,b), styrene oligomers were formed, but to a lower extent than over the n-ZSM-5 ( Figure 3c)a nd ZrO 2 /n-ZSM-5 ( Figure 3d)c atalysts. The intensity evolution of the cyclic oligomers (7), favored in zones with high densities of Brønsted acid sites, was particularly low for the ZrO 2 /n-ZSM-5-ATPc atalyst. On the contrary,t he formation of linear dimer (5) was more pronounced, especially in the first 5min of the reaction;a fterwards, the relative amount of trimero ligomers (6a and 6b)i ncreased.…”
Section: Catalyst Propertiesmentioning
confidence: 95%
“…The optimum conditions for maximizing the yield of the liquid fraction (bio-oil) comprise intermediate temperatures, typically in the range 500-600 8C, and high heatingr ates (fast pyrolysis). [2,[5][6][7][8][9] In most cases, these transformations are aimed to reduce( at least partially) the oxygen content of the bio-oil, thus bringing its chemical compositionc loser to that typical of fossil-derived fuels. [4] Bio-oil upgradinghas been investigated by avariety of physical and chemical methods.…”
Section: Introductionmentioning
confidence: 99%
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“…This is the first study in which fast pyrolysis is comparatively 163 assessed with catalytic pyrolysis for olive husk/kernels. (Deng et al 2006, Gaertner et al 2009, Mante et al 2015, Snell et al 2010). Prior to the 194 experiments, the catalytic materials were calcined at 500 °C for 3 h and stored in a desiccator.…”
mentioning
confidence: 99%
“…The MgO (5% Co) catalyst that are catalysed by the basic sites of the catalyst (Deng et al 2009, Snell et al 2010). …”
mentioning
confidence: 99%