2004
DOI: 10.1016/j.molcata.2003.09.015
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Alkylation of p-cresol with tert-butanol catalyzed by heteropoly acid supported on zirconia catalyst

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Cited by 62 publications
(38 citation statements)
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“…The another reason is due to lower deactivation caused in supercritical CO 2 compared to conventional organic solvents [3]. The yield of 2,6-DTBPC (53%) observed for HPW(30)/MCM-41 was the highest yield ever observed in literature: the maximum yield of DTBC was 20% in the vapor phase reaction [14]. The t-butylation of p-cresol over relatively weaker HSiW the support for highly dispersed HPW, and provides the reaction circumstances for the formation of bulky 2,6-DTBPC by the cooperation of strong acid.…”
Section: Resultsmentioning
confidence: 99%
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“…The another reason is due to lower deactivation caused in supercritical CO 2 compared to conventional organic solvents [3]. The yield of 2,6-DTBPC (53%) observed for HPW(30)/MCM-41 was the highest yield ever observed in literature: the maximum yield of DTBC was 20% in the vapor phase reaction [14]. The t-butylation of p-cresol over relatively weaker HSiW the support for highly dispersed HPW, and provides the reaction circumstances for the formation of bulky 2,6-DTBPC by the cooperation of strong acid.…”
Section: Resultsmentioning
confidence: 99%
“…Alkylation of p-cresol with t-butanol produces industrially important organic intermediates, such as 2-t-butyl-4-methylphenol (2-TBPC) and 2,6-di-tbutyl-4-methylphenol (2,6-DTBPC), which are widely used in antioxidants and polymerization inhibitors and in the manufacture of phenol resins [7]. Recently, many workers have been attention to the liquid phase or vapor phase t-butylation of phenols over solid acid catalysts, such as zeolites [9][10][11], clays [12], metal oxides [13], and mesoporous materials [14][15][16][17][18][19][20] including their modified catalysts; however, there have been a few to succeed in the di-t-butylation of phenols. We have considered one of the reasons is the deactivation of acidic sites by coke formation.…”
Section: Introductionmentioning
confidence: 99%
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“…But the catalyst deactivated due to the leaching of active sites [ 32 ]. For tert -butylation of p -cresol with tert -butanol, 15 % PTA/ZrO 2 (calcined at 750 °C) was also studied under continuous down-fl ow conditions [ 33 ]. The catalyst gave good p -cresol conversion (~60 %) and high selectivity (~90 %) for TBC.…”
Section: Veratrole Acylation With Benzoic Anhydridementioning
confidence: 99%
“…The traditional catalysts include sulfate, phosphate [5,6], cation exchange resin [7], SO 4 2-/ZrO 2 supported on HMS [8] and heteropolyacid supported on ZrO 2 [9]. However these catalysts more or less have the shortcomings of large dosage, strong corrosion, complex post-treatment technology, environmental pollution, deep colored products and poor reproducibility.…”
Section: Choice and Preparation Of The Catalystmentioning
confidence: 99%