This website uses cookies to give you the best user experience. If you continue
without changing your settings we'll assume you are happy to receive all RSC cookies.
You can change your cookie settings by navigating to our Privacy and Cookies page and following the instructions. These instructions
are also obtainable from the privacy link at the bottom of any RSC page.
Department of Chemical and Biological Engineering, University of Wisconsin-Madison, 1415 Engineering Drive, Madison, USA
E-mail: dumesic@engr.wisc.edu
; Fax: 1 608 262 5434
; Tel: 1 608 262 1095
Green Chem., 2010,12, 223-227
DOI:
10.1039/B920369A
Received
30 Sep 2009,
Accepted
25 Nov 2009
First published online
13 Jan 2010
Mono-functional intermediates produced by catalytic conversion of sugars and polyols over Pt–Re/Ccatalysts (consisting of alcohols, ketones, carboxylic acids, and heterocyclic compounds) can be upgraded to fuel-grade compounds using two catalytic reactors operated in a cascade mode. The first reactor achieves C–C coupling of mono-functional intermediates using a dual-bed catalyst system, where the upstreamcatalyst bed (Ce1Zr1Ox) is employed to carry out ketonization of carboxylic acids, and the downstreamcatalyst bed (Pd/ZrO2) is used to achieve aldol condensation/hydrogenation of alcohols and ketones. This second bed is not significantly inhibited by CO2 and H2O produced during ketonization. The high molecular weight ketones produced by C–C coupling reactions in the dual-bed catalyst system are subsequently converted to alkanes by hydrodeoxygenation (i.e., dehydration/hydrogenation) over a Pt/SiO2–Al2O3catalyst. Using the aforementioned approach, an aqueous feed containing 60 wt% sorbitol was converted to a liquid stream of alkanes, 53% of which consisted of C7+ alkanes with minimal branching, desirable for Diesel fuel.
Fetching data from CrossRef. This may take some time to load.