2009
DOI: 10.1134/s0023158409030112
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Catalytic properties of antimony-SBA-15 materials in the benzylation of aromatics reactions

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Cited by 6 publications
(6 citation statements)
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“… [a] Ageing temperature; [b] Final zirconium loading measured by using ICP–OES, with incorporation efficiency in parentheses; [c] Total pore volume; [d] Micropore volume; [e] “Accessible” pore volume; [f] Pore size calculated as the maximum of pore size distribution calculated by using the BJH method using a nitrogen multilayer thickness curve specifically obtained for SBA‐15 materials;47 [g] Surface area calculated from the BET method; [h] Micropore surface area; [i] “Accessible” surface area for mesopores/macropores; [j] Interplanar spacing calculated as d 100 =( d 100 +√3⋅ d 110 +√4⋅ d 200 )/3; [k] The p 6 mm lattice parameter a =2⋅ d 100 /√3; [l] Wall thickness; [m] Acid loading calculated from NH 3 TPD profiles; [n] Maximum temperature of the NH 3 desorption profile; [o] Active surface area calculated from H + by using 0.14 nm 2 molecule −1 for the average cross‐sectional area of NH 3 ; [p] Accessibility of supported acid zirconium species, calculated as the specific number of acid sites per zirconium content. …”
Section: Resultsmentioning
confidence: 99%
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“… [a] Ageing temperature; [b] Final zirconium loading measured by using ICP–OES, with incorporation efficiency in parentheses; [c] Total pore volume; [d] Micropore volume; [e] “Accessible” pore volume; [f] Pore size calculated as the maximum of pore size distribution calculated by using the BJH method using a nitrogen multilayer thickness curve specifically obtained for SBA‐15 materials;47 [g] Surface area calculated from the BET method; [h] Micropore surface area; [i] “Accessible” surface area for mesopores/macropores; [j] Interplanar spacing calculated as d 100 =( d 100 +√3⋅ d 110 +√4⋅ d 200 )/3; [k] The p 6 mm lattice parameter a =2⋅ d 100 /√3; [l] Wall thickness; [m] Acid loading calculated from NH 3 TPD profiles; [n] Maximum temperature of the NH 3 desorption profile; [o] Active surface area calculated from H + by using 0.14 nm 2 molecule −1 for the average cross‐sectional area of NH 3 ; [p] Accessibility of supported acid zirconium species, calculated as the specific number of acid sites per zirconium content. …”
Section: Resultsmentioning
confidence: 99%
“…The alkylation of aromatics with benzyl chloride has been reported to be primarily catalyzed by Lewis acid sites 46. 47 The results are summarized in Table 2 and illustrated in Figure 6. The reaction proceeded smoothly for all materials in a short reaction time (typically 5 min).…”
Section: Resultsmentioning
confidence: 99%
“…H2SO4, HCl, HNO3) are most frequently used in the synthesis of benzylated arenes, 8 however, they cause sever environmental issues and problems with catalyst separation and regeneration. 9 Environmentally friendly heterogeneous catalysts have been developed to replace homogeneous acids, including zeolites and mesoporous silica-alumina, 7,[10][11][12][13][14][15][16][17][18][19][20][21][22] acidic oxides and sulphides, [23][24][25][26][27][28][29][30] and heteropoly acids (HPAs). 15,31 Zeolites, having crystalline framework, high surface area, regular porous structure, and strong acidity, are the most popular catalysts used in current chemical processes.…”
Section: ◼ Introductionmentioning
confidence: 99%
“…Three probable mechanistic interpretations can be found in the literature for benzylation of aromatic hydrocarbons with benzyl chloride on solid acid based supported metal catalysts, without any direct (preparative or spectroscopic) experimental verification: a simple radical step [12][13][14][15][16][17] -see Scheme 1; the presence of a benzyl chloride radical cation [4,[18][19][20][21][22][23][24][25]] -see Scheme 2; or the presence of a benzyl radical cation [26][27][28] as intermediate -see Scheme 3. In some cases the same authors have different suggestions for similar catalytic systems.…”
Section: Introductionmentioning
confidence: 99%