Zeolite Beta, modified with some salts of alkali and alkaline earth metals (K, Zn, Sn), were tested in the hydrothermal heterogeneous catalytic decomposition of microcrystalline cellulose. The reactions were microwave-assisted, where the microwaves were issued by an in-situ coaxial applicator. Zeolites were submitted to an ion-exchange process which determines a loss of crystallinity in the following order: Sn-Beta-IE > K-Beta > Zn-Beta > acid form H-Beta. The interaction between zeolites and microwaves was studied by irradiating zeolite powder under constant power and the heating response was in the following order: K-Beta > NH4-Beta > Sn-Beta-IE ? Zn-Beta > H-Beta > Alumina. These results show that the nature of counterion strongly affects the absorption of microwaves. The catalytic activity of the different systems on the cellulose decomposition was studied, and resulted in the following order: H-Beta > K-Beta > Zn-Beta > Sn-Beta-IE > Alumina, when the reaction media contained 5mM HCl. The most active catalyst was the acid zeolite Beta and the identified product distribution under the investigated conditions was (mol yield %): Levulinic acid (22.3), Glucose (12.1), Lactic acid (4.1), Formic acid (6.6), 5-(Hydroxymethyl) furfural (14.6), Acetic acid (15.2) and Furfuraldehyde (3.1). The effect of temperature, time and the heterogeneous catalyst recycling (H-Beta) on the yields of different products was investigated. The use of MW radiation with coaxial applicator instead of conventional heating gave clear advantages in the decrease of the reaction time (45 min) and in terms of yield enhancement (78.6% in the best conditions).

Heterogeneous catalytic reaction of microcrystalline cellulose in hydrothermal microwave assisted decomposition: effect of modified zeolite Beta

M Onor;E Bramanti;I Longo;C Ferrari
2014

Abstract

Zeolite Beta, modified with some salts of alkali and alkaline earth metals (K, Zn, Sn), were tested in the hydrothermal heterogeneous catalytic decomposition of microcrystalline cellulose. The reactions were microwave-assisted, where the microwaves were issued by an in-situ coaxial applicator. Zeolites were submitted to an ion-exchange process which determines a loss of crystallinity in the following order: Sn-Beta-IE > K-Beta > Zn-Beta > acid form H-Beta. The interaction between zeolites and microwaves was studied by irradiating zeolite powder under constant power and the heating response was in the following order: K-Beta > NH4-Beta > Sn-Beta-IE ? Zn-Beta > H-Beta > Alumina. These results show that the nature of counterion strongly affects the absorption of microwaves. The catalytic activity of the different systems on the cellulose decomposition was studied, and resulted in the following order: H-Beta > K-Beta > Zn-Beta > Sn-Beta-IE > Alumina, when the reaction media contained 5mM HCl. The most active catalyst was the acid zeolite Beta and the identified product distribution under the investigated conditions was (mol yield %): Levulinic acid (22.3), Glucose (12.1), Lactic acid (4.1), Formic acid (6.6), 5-(Hydroxymethyl) furfural (14.6), Acetic acid (15.2) and Furfuraldehyde (3.1). The effect of temperature, time and the heterogeneous catalyst recycling (H-Beta) on the yields of different products was investigated. The use of MW radiation with coaxial applicator instead of conventional heating gave clear advantages in the decrease of the reaction time (45 min) and in terms of yield enhancement (78.6% in the best conditions).
2014
Istituto di Chimica dei Composti OrganoMetallici - ICCOM -
Istituto Nazionale di Ottica - INO
levulnic acid
solid acid
conversion
hydrolysis
glucose
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Utilizza questo identificativo per citare o creare un link a questo documento: https://hdl.handle.net/20.500.14243/263652
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