4.7 Article

Preparation of Metal-Acid bifunctional catalyst Ni/ZSM-22 for palmitic acid catalytic deoxygenation

Journal

FUEL
Volume 332, Issue -, Pages -

Publisher

ELSEVIER SCI LTD
DOI: 10.1016/j.fuel.2022.126139

Keywords

Bio-oil; Hydrodeoxygenation; Palmitic acid; Bifunctional Catalyst

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In this study, Ni-based ZSM-22 catalysts were successfully prepared by combining ethanol dispersion with rotary evaporation. The catalyst, denoted as Ni/Z22@E, exhibited improved catalytic activity in palmitic acid deoxygenation compared to the wet-impregnated method. The conversion of palmitic acid reached 98.9%, with a high C16/C15 alkane ratio of 4.07. The stability of the Ni species on the catalyst surface prevented deactivation due to coking or leaching. The mechanism and kinetics of the reaction were analyzed, showing that the ethanol dehydration reaction was the most difficult to occur. The high selectivity for C16 alkanes was attributed to the low activation energy of the hydrodeoxygenation pathway. Additionally, a mechanistic change in the fatty acid deoxygenation reaction was observed at around 240 degrees C, leading to a significant increase in the hydrodecarboxylation pathway.
In this work, methods employing ethanol for dispersion as well as precursor combination by rotary evaporation were combined to produce Ni-based ZSM-22 catalysts. The catalytic activity in palmitic acid deoxygenation over Ni/Z22@E was enhanced compared with that of the wet-impregnated method. The conversion of palmitic acid reached 98.9 %, in which C16/C15 alkane was as high as 4.07. The Ni species on the surface of catalysts showed strong stability so that not susceptible to inactivation by coking or leaching. In addition, the mechanism and kinetics of the palmitic acid deoxygenation reaction were analyzed. The results showed that the ethanol dehy-dration reaction was the most difficult to occur, and the high C16 alkanes selectivity can be attributed to the low activation energy of the hydrodeoxygenation (HDO) pathway. Both experimental and kinetics calculation results suggested that there may be a mechanistic change in the fatty acid deoxygenation reaction at around 240 degrees C that resulted in a large increase in the hydrodecarboxylation (HDX) pathway. Based on this, selected adjustments of the products were proposed for fatty alcohols below 220 degrees C, C16 alkanes between 260 and 280 degrees C, and C15 al-kanes above 280 degrees C.

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