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Détail de l'auteur
Auteur Rajesh Gopinath
Documents disponibles écrits par cet auteur
Affiner la rechercheCatalytic hydrogenolysis of glycerol to propylene glycol over mixed oxides derived from a hydrotalcite-type precursor / Lekha Charan Meher in Industrial & engineering chemistry research, Vol. 48 N°4 (Février 2009)
[article]
in Industrial & engineering chemistry research > Vol. 48 N°4 (Février 2009) . - pp. 1840–1846
Titre : Catalytic hydrogenolysis of glycerol to propylene glycol over mixed oxides derived from a hydrotalcite-type precursor Type de document : texte imprimé Auteurs : Lekha Charan Meher, Auteur ; Rajesh Gopinath, Auteur ; S. N. Naik, Auteur Année de publication : 2009 Article en page(s) : pp. 1840–1846 Note générale : Chemical engineering Langues : Anglais (eng) Mots-clés : Propylene glycol Glycerol Hydrogenolysis Cu/Zn/Al mixed-metal oxide catalysts Résumé : Selective hydrogenolysis of glycerol to propylene glycol was performed using an environmentally friendly hydrotalcite-derived mixed-metal oxide catalyst. The Mg/Al, Zn/Al, Ni/Mg/Al, Ni/Co/Mg/Al, and Cu/Zn/Al mixed-metal oxide catalysts were prepared from their corresponding hydrotalcite precursors having M2+/M3+ compositions over the range of 0.5−3.0. The physicochemical properties of the catalysts were studied by X-ray diffraction (XRD), inductively coupled plasma mass spectrometry (ICP-MS), NH3 and CO2 temperature-programmed desorption (TPD), and nitrogen adsorption studies. The XRD patterns of pure hydrotalcites exhibited characteristics of hydrotalcite phases, while those of calcined hydrotalcites showed the formation of corresponding metal oxides. The ICP-MS analysis showed agreement between the calculated and actual metal compositions. The prepared catalysts were evaluated for the hydrogenolysis of glycerol to propylene glycol in a Parr reactor. The activity studies indicated a maximum glycerol conversion and selectivity toward propylene glycol in the case of Cu/Zn/Al mixed-metal oxide catalysts. Further, the reaction parameters were optimized with the most active Cu/Zn/Al catalyst, and it was found that at a catalyst concentration of 5% (w/w) of aqueous glycerol, a hydrogen pressure of 200 psig, and 80% glycerol dilution, a maximum glycerol conversion of 52% with 93−94% selectivity toward propylene glycol were obtained. En ligne : http://pubs.acs.org/doi/abs/10.1021/ie8011424 [article] Catalytic hydrogenolysis of glycerol to propylene glycol over mixed oxides derived from a hydrotalcite-type precursor [texte imprimé] / Lekha Charan Meher, Auteur ; Rajesh Gopinath, Auteur ; S. N. Naik, Auteur . - 2009 . - pp. 1840–1846.
Chemical engineering
Langues : Anglais (eng)
in Industrial & engineering chemistry research > Vol. 48 N°4 (Février 2009) . - pp. 1840–1846
Mots-clés : Propylene glycol Glycerol Hydrogenolysis Cu/Zn/Al mixed-metal oxide catalysts Résumé : Selective hydrogenolysis of glycerol to propylene glycol was performed using an environmentally friendly hydrotalcite-derived mixed-metal oxide catalyst. The Mg/Al, Zn/Al, Ni/Mg/Al, Ni/Co/Mg/Al, and Cu/Zn/Al mixed-metal oxide catalysts were prepared from their corresponding hydrotalcite precursors having M2+/M3+ compositions over the range of 0.5−3.0. The physicochemical properties of the catalysts were studied by X-ray diffraction (XRD), inductively coupled plasma mass spectrometry (ICP-MS), NH3 and CO2 temperature-programmed desorption (TPD), and nitrogen adsorption studies. The XRD patterns of pure hydrotalcites exhibited characteristics of hydrotalcite phases, while those of calcined hydrotalcites showed the formation of corresponding metal oxides. The ICP-MS analysis showed agreement between the calculated and actual metal compositions. The prepared catalysts were evaluated for the hydrogenolysis of glycerol to propylene glycol in a Parr reactor. The activity studies indicated a maximum glycerol conversion and selectivity toward propylene glycol in the case of Cu/Zn/Al mixed-metal oxide catalysts. Further, the reaction parameters were optimized with the most active Cu/Zn/Al catalyst, and it was found that at a catalyst concentration of 5% (w/w) of aqueous glycerol, a hydrogen pressure of 200 psig, and 80% glycerol dilution, a maximum glycerol conversion of 52% with 93−94% selectivity toward propylene glycol were obtained. En ligne : http://pubs.acs.org/doi/abs/10.1021/ie8011424