2004
DOI: 10.1016/j.crci.2003.12.006
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Selective glycerol transesterification over mesoporous basic catalysts

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Cited by 49 publications
(27 citation statements)
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“…This non-reactivity of siliceous materials at 110 8C was attributed to strong hydrophilic interactions between the siliceous surface and glycerol. Indeed, as described for the MgAlMCM-41 catalyst, [44] glycerol was strongly adsorbed on the siliceous surface and at 110 8C hydrophilic interactions were strong enough to avoid the approach of the fatty methyl esters to the catalytic sites.…”
Section: Organic and Organic-inorganic Materialsmentioning
confidence: 96%
See 1 more Smart Citation
“…This non-reactivity of siliceous materials at 110 8C was attributed to strong hydrophilic interactions between the siliceous surface and glycerol. Indeed, as described for the MgAlMCM-41 catalyst, [44] glycerol was strongly adsorbed on the siliceous surface and at 110 8C hydrophilic interactions were strong enough to avoid the approach of the fatty methyl esters to the catalytic sites.…”
Section: Organic and Organic-inorganic Materialsmentioning
confidence: 96%
“…[44] As described earlier (part c, Section 2.2.1.) for esterifications, [27][28][29][30][31][32] a significant hindrance of the porous framework is expected to induce a shape-selectivity effect.…”
Section: B Metal Oxides Dispersed Over Mesoporous Silicamentioning
confidence: 97%
“…Suppes et al [53] similarly commented that the liquid phase transesterification benefits from larger pore structures but not as much from the high surface area created by the inner pore structures of zeolites. The emphasis on large pore structure naturally motivated the utilization of mesoporous zeolites such as SBA-15 and MCM-41 [58,67,68].…”
Section: Zeolitementioning
confidence: 99%
“…In addition to the use in the esterification of FFAs in vegetable oils and animal fats, heterogeneous acid catalysts for biodiesel synthesis could in principle be employed to catalyze the simultaneous reactions of TGs and FFAs with low molecular alcohols in transesterification and esterification, respectively [3]. Among the heterogeneous acid catalysts studied to date for trans/esterification are zeolites [4,5], MCM-41 [6,7], tungstated zirconia [8][9][10], sulfated zirconia [11][12][13][14], Amberlyst-15 [15][16][17] and Nafion [18][19][20][21][22]. Some common problems with solid acid catalysts have been: low acid site concentrations, microporosity, hydrophilic character of catalyst surfaces, and active site leaching.…”
Section: Introductionmentioning
confidence: 99%