2019•ACS Sustainable Chemistry & EngineeringRequires access

Hydrodeoxygenation (HDO) of Biomass Derived Ketones Using Supported Transition Metals in a Continuous Reactor

Xiaokun Yang, Rhodri W. Jenkins, Juan H. Leal, Cameron M. Moore, Elizabeth J. Judge, Troy A. Semelsberger, Andrew D. Sutton

Open publisher page 24 citations

Abstract

The hydrodeoxygenation (HDO) of 5-nonanone—a model compound for more complex biomass-derived molecules—to n -nonane was investigated using a variety of heterogeneous multifunctional metal-impregnated aluminosilicate catalysts in a packed-bed continuous flow reactor system. Under optimized reaction conditions (200 °C, 1.38 MPa H 2 ), >99% conversion and >99% selectivity to n -nonane was achieved within a 30 min residence time over both Ni (7 wt %) and Co (9 wt %) supported on Perlkat 79-3, a high-surface area amorphous aluminosilicate. This work provides a further understanding of the effects of different metals, supports, and metal loading amounts on HDO of 5-nonanone and demonstrates an efficient translation of HDO reactions of ketones from batch reactors to continuous flow systems.

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What this paper is about

The hydrodeoxygenation (HDO) of 5-nonanone—a model compound for more complex biomass-derived molecules—to n -nonane was investigated using a variety of heterogeneous multifunctional metal-impregnated aluminosilicate catalysts in a packed-bed continuous flow reactor system. Under optimized reaction conditions (200 °C, 1.38 MPa H 2 ), >99% conversion and >99% selectivity to n -nonane was achieved within a 30 min residence time over both Ni (7 wt %) and Co (9 wt %) supported on Perlkat 79-3, a high-surface area amorphous aluminosilicate. This work provides a further understanding of the effects of different metals, supports, and metal loading amounts on HDO of 5-nonanone and demonstrates an efficient translation of HDO reactions of ketones from batch reactors to continuous flow systems.

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Available abstract

The hydrodeoxygenation (HDO) of 5-nonanone—a model compound for more complex biomass-derived molecules—to n -nonane was investigated using a variety of heterogeneous multifunctional metal-impregnated aluminosilicate catalysts in a packed-bed continuous flow reactor system. Under optimized reaction conditions (200 °C, 1.38 MPa H 2 ), >99% conversion and >99% selectivity to n -nonane was achieved within a 30 min residence time over both Ni (7 wt %) and Co (9 wt %) supported on Perlkat 79-3, a high-surface area amorphous aluminosilicate. This work provides a further understanding of the effects of different metals, supports, and metal loading amounts on HDO of 5-nonanone and demonstrates an efficient translation of HDO reactions of ketones from batch reactors to continuous flow systems.

Key concepts: Hydrodeoxygenation, Catalysis, Chemistry, Aluminosilicate, Nonane, Transition metal, Microreactor, Residence time (fluid dynamics)

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