We explore a glycerol-to-olefins process in a reactor containing dehydration, hydrogenation, and upgrading stages in series. Glycerol, co-fed with H-2 over HZSM-5 (1.0 g, Si/AI = 11.5, 400 degrees C), was first dehydrated to yield a mixture of acetaldehyde, acrolein, and hydroxypropanone. Acrolein was hydrogenated to propanal over a Pd/alpha-Al2O3 catalyst and the effluent was passed to a third stage which served to further upgrade propanal to olefins. Rapid third stage deactivation was observed, although, we obtained a maximum 70% yield of light olefins from a propanal stream reacted over HBEA (0.5 g, 500 degrees C) with minimal CO production. A decrease in propanal conversion and C2-3 olefin yield was observed along with a corresponding increase in C4-5 olefin yield as time-on-stream increased to 150 min. We conclude that propanal condensed over Bronsted acid sites to form C4-5 olefins, which subsequently cracked at high conversion to form C2-3 olefins. Increasing the temperature from 400 to 500 degrees C also decreased the C4-5 olefin yield from 13 to 9% while increasing C2-3 olefin yield from 4 to 15%. C-C bond formation occurred during glycerol upgrading in a staged reactor configuration and negligible carbon is lost as CO. (C) 2014 Elsevier B.V. All rights reserved.