Yadav, Ganapati D. ; Salgaonkar, Sanket S. (2005) Selectivity engineering of 2,6-diisopropylphenol in isopropylation of phenol over Cs2.5H0.5PW12O40/K-10 clay Industrial & Engineering Chemistry Research, 44 (6). pp. 1706-1715. ISSN 0888-5885
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Official URL: http://pubs.acs.org/doi/abs/10.1021/ie049141q
Related URL: http://dx.doi.org/10.1021/ie049141q
Abstract
Propofol (2,6-diisopropylphenol), a very important drug, is typically synthesized by the isopropylation of phenol over an acid catalyst. This process consists of two series reactions, namely, the formation of 2-isopropylphenol and its further isopropylation to 2,6- and 2,4-diisopropylphenols. The selectivity to 2,6-diisopropylphenol depends on a number of parameters, and the alkylating agent, type of catalyst, and temperature play a major role. With 2-propanol (IPA) as the alkylating agent, its dehydration to propylene and the subsequent formation of isopropyl ether (DIPE) need to be considered. The fact that isopropyl ether, formed in situ, is itself a good alkylating agent further complicates the reaction network. Modeling this intricate system requires extensive experimental data free from mass-transfer limitations. Thus, the alkylation of both phenol and monoisopropylphenol was studied in the liquid phase in an autoclave at 200 °C using IPA and DIPE independently as alkylating agents, over 20% (w/w) Cs2.5H0.5PW12O40/K-10 catalyst, which is a synergistic combination of cesium-modified heteropolyacid and clay. This catalyst is better than zeolites reported in the literature. The effect of various operating parameters and catalyst reusability was also investigated. Mathematical models were proposed to probe into the intricate reaction kinetics and mechanism consistent with the experimental results.
Item Type: | Article |
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Source: | Copyright of this article belongs to American Chemical Society. |
ID Code: | 111758 |
Deposited On: | 15 Sep 2017 13:04 |
Last Modified: | 15 Sep 2017 13:04 |
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