Abstract
In this work the acid-catalysed reactions involved in the one-pot production of pentyl valerate (PV) from γ-valerolactone (GVL) and pentanol in liquid phase at 523 K, 10 bar of N 2 over acidic catalysts was studied. Two consecutive acid-catalysed reactions must be performed: (1) nucleophilic addition of pentanol (PL) to GVL to form 4-hydroxy pentyl valerate (HPV) and (2) HPV dehydration into pentyl 2-pentenoate (PP), avoiding the undesirable formation of 4-pentoxy pentyl valerate (PPV). It was found that the support activity and selectivity strongly depended on: (i) the nature; (ii) strength; (iii) density of acid sites and (iv) the textural properties of the acid support. Solids containing predominantly Lewis acid sites, such as ZnO/SiO 2 , γ-Al 2 O 3 and NaY zeolite promote mainly a strong GVL adsorption leading to a relatively high missing carbon balance. Catalysts having mainly surface Brønsted acid sites of medium–high strength, such as HPA/SiO 2 , showed a very high activity and selectivity to PP but deactivated dramatically. Zeolites containing at least 40% of Brønsted acidity and strong acid sites promoted remarkably the undesirable intramolecular dehydration of pentanol into pentenes. SiO 2 -Al 2 O 3 , exhibiting a B/(L + B) ratio of 0.21 and a wide strength of acid sites, was more selective to PP than to PPV though the missing carbon balance was high. By calorimetric adsorption and temperature-programmed oxidation adsorption enthalpies of 61.9 and 59.1 Kcal/mol for GVL and PL were obtained, respectively. Besides, by temperature-programmed desorption experiments it was determined that GVL adsorption is irreversible on SiO 2 -Al 2 O 3 , whereas in the case of PL is partially reversible. The effect of the calcination temperature on the product distribution and evolution of the missing carbon balance was also studied over SiO 2 -Al 2 O 3 . These results contribute to the future design of more efficient bifunctional catalytic systems for biofuel production.
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