Abstract
Over the past decades, impending oil shortages combined
with petroleum market instability have prompted a search for
a new source of both transportation fuels and bulk chemicals.
Renewable bio-based feedstocks such as sugars, grains, and
seeds are assumed to be capable of contributing to a significant
extent as fuel and bulk chemical sources.[1] However,
utilization of these new types of high-oxygen-content feeds as
either fuels or bulk chemical precursors is not trivial.
Triglyceride or fatty acid feeds have the potential to be used
as fuel because of their structural resemblance to diesel-type
hydrocarbons, but further processing is required to reduce
their high-oxygen content and related acidity.[2] This goal is
typically achieved by hydroprocessing, thus resulting in
deoxygenation (DO) of the triglyceride/fatty acid feed and
yielding either saturated hydrocarbons suitable for diesel fuel,
or linear olefins suitable for bulk chemical precursors.
Although extensive studies have been done on deoxygenation
of biomass-related feeds,[2, 3] catalyst research has so far
been limited to supported noble-metal catalysts known for
their hydrogenation activity and standard hydrodesulfurization
(HDS) catalysts. The use of HDS catalysts can be
problematic since catalyst deactivation resulting from sulfur
leaching will result in contamination of the product stream.[4]
The major drawback of noble-metal catalysts is their limited
availability. Herein we demonstrate the use of tungsten-based
catalysts for the deoxygenation of triglyceride-based feedstocks.
Changes in a (pre)treatment procedure are shown to
control catalyst selectivity, thus allowing high yields of
unsaturated products even in the presence of hydrogen.
| Original language | English |
|---|---|
| Pages (from-to) | 5089-5092 |
| Number of pages | 4 |
| Journal | Angewandte Chemie-International Edition |
| Volume | 52 |
| Issue number | 19 |
| DOIs | |
| Publication status | Published - 2013 |