Hydrotalcite as active and selective catalyst for synthesis of dehydrozingerone from vanillin and acetone: effect of catalyst composition and calcination temperature on activity and selectivity

Bhanawase, Shivaji ; Yadav, Ganapati (2017) Hydrotalcite as active and selective catalyst for synthesis of dehydrozingerone from vanillin and acetone: effect of catalyst composition and calcination temperature on activity and selectivity Current Catalysis, 6 (2). pp. 105-114. ISSN 2211-5447

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Official URL: http://www.eurekaselect.com/147618/article

Related URL: http://dx.doi.org/10.2174/2211544705666161123122411

Abstract

Background: Dehydrozingerone is a biosynthetic intermediate and structural analog of curcumin. It is a flavoring ingredient and has antioxidant and antimutagenic properties. Dehydrozingerone can be efficiently synthesized from vanillin and acetone by cross-aldol (or Claisen-Schmidt) condensation using heterogeneous base catalysts. Vanillin can be sourced from the valorization of biomass. Green chemistry aspects such as 100 % atom economy and low E factor are very important in any synthesis which could be achieved by use of heterogeneous catalysis. Methods: Hydrotalcites with different Mg: Al ratio were synthesized and calcined in air at 450 ºC and 500 ºC to understand the effect of catalyst composition and calcination temperature on activity and selectivity in the synthesis of dehydrozingerone from vanillin and acetone. All catalysts were characterized by different techniques such as XRD, FTIR, ASAP, TPD, TEM and SEM-EDXS. Effects of various process parameters were studied to establish reaction mechanism and kinetics. The kinetic model was validated by experimental data. The product was confirmed by GC-MS and 1H NMR. Results: Among all catalysts, hydrotalcite of Mg: Al of mole ratio 3:1, calcined at 500 ºC for 6 h (31CHT500) was found active, selective and reusable. Hydrotalcite calcined at 500 ºC gave mixed Mg- Al metal oxides. Dehydrozingerone was efficiently obtained with 100 % selectivity at vanillin conversion of 88 % over 31CHT500 at 130 ºC after 4 h. A pseudo first order kinetics was found to fit the data well. Conclusion: Catalyst composition and calcination temperature were affecting the activity of catalysts. Temperature, catalyst loading and vanillin to acetone mole ratio were influencing the reaction rate. Maximum yield of dehydrozingerone was obtained at following reaction conditions: temperature, 130 ºC; amount of catalyst, 0.015 g mL−1; mole ratio of vanillin: acetone, 1:15; autogenous pressure, 10 atm. All species were weakly adsorbed on catalytic sites. The reaction was pseudo first order with apparent activation energy of 9.4 kcal mol-1. Dehydrozingerone was synthesized from vanillin and acetone by a green process.

Item Type:Article
Source:Copyright of this article belongs to Bentham Science Publishers.
Keywords:Biomass; Vanillin; Hydrotalcite; Dehydrozingerone; Cross-Aldol (or Claisen-Schmidt); Condensation
ID Code:110705
Deposited On:15 Sep 2017 13:21
Last Modified:15 Sep 2017 13:21

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