New catalysts of Pt, PtNi, PtCo, and NiCo supported on Al 2 O 3 were developed for producing hydrogen by aqueous phase reforming (APR) of oxygenated hydrocarbons. e urea matrix combustion technique was used for loading the metal on the support in order to improve several aspects: increase both the metal-support interaction and the metal dispersion and decrease the metal load. e catalysts were characterized by MS/ICP, N 2 adsorption, XRD, TPR, CO chemisorption, and the test of cyclohexane dehydrogenation (CHD). e APR of a solution of 10% mass ethylene glycol (EG), performed in a tubular fixed bed reactor at 498 K, 22 bar, WHSV � 2.3 h −1 , was used as the main reaction test. After 10 h on-stream, the catalysts prepared by UMC had better hydrogen yield and catalytic stability than common catalysts prepared by IWI. e UMC/IWI H 2 yield ratio was 23.5/15.2 for Pt, 24.0/17.0 for PtCo, 26.6/21.0 for PtNi, and 8.0/3.9 for NiCo. Ni or Co addition to Pt increased the carbon conversion while keeping the H 2 turnover high. Cobalt also improves stability. Reports of several authors were revised for a comparison. e analysis indicated that the developed catalysts are a viable and cheaper alternative for H 2 production from a renewable resource.