In total 17 heterogeneous catalysts, with combinations of 4 transition metals (Ni, Ru, Cu and Co) and various promoters (e.g., Na, K, Mg, or Ru) supported on different materials (gamma-Al(2)O(3), ZrO(2), and activated carbon (AC)), were investigated with respect to their catalytic activity and stability for H(2) production from glucose via supercritical water gasification (SCWG). The experiments were carried out at 600 degrees C and 24 MPa in a bench-scale continuous-flow tubular reactor. Ni (in metallic form) and Ru (in both metallic and oxidized forms) supported on gamma-Al(2)O(3) exhibited very high activity and H2 selectivity among all of the catalysts investigated for a time-on-stream of 5-10 h. With Ni20/gamma-Al(2)O(3) (i.e., gamma-Al(2)O(3) with 20 wt% Ni), a H(2) yield of 38.4 mol/kg glucose was achieved, approximately 20 times higher than that obtained during the blank test without catalyst (1.8 mol/kg glucose). In contrast, Cu and Co catalysts were much less effective for glucose SCWG reactions. As for the effects of catalyst support materials on activity, the following order of sequence was observed: gamma-Al(2)O(3) > ZrO(2) > AC. In addition, Mg and Ru were found to be effective promoters for the Ni/gamma-Al(2)O(3) catalyst, suppressing coke and tar formation. Copyright (C) 2011, Hydrogen Energy Publications, LLC. Published by Elsevier Ltd. All rights reserved.