in Wiley Online Library (wileyonlinelibrary.com)Biomass gasification gas contains condensable hydrocarbons usually referred to as "tars." The use of chemical-looping reforming (CLR) has been proposed as a downstream technology for tar removal. The tar removal capabilities and the regeneration properties of two particularly promising bed materials, CuO/MgAl 2 O 4 and La 0.8 Sr 0.2 FeO 3 /c-Al 2 O 3 , were investigated using C 2 H 4 , C 6 H 6 , and C 7 H 8 as tar surrogates. The material La 0.8 Sr 0.2 FeO 3 /c-Al 2 O 3 exhibited high levels of conversion of all tar surrogates investigated, whereas CuO/MgAl 2 O 4 showed less promising behavior. For this material, the C 2 H 4 conversion in the absence of aromatic compounds was very high, but in the presence of monoaromatic compounds, the conversion of aromatics and C 2 H 4 was poor. This indicates that monoaromatic compounds hinder the conversion of C 2 H 4 effectively. Therefore, C 2 H 4 may not always be a good choice as a tar surrogate and its suitability may depend on the mechanism of hydrocarbon conversion on the bed material surface in question. Composition 40 wt % CuO, 60 wt % MgAl 2 O 4 (Baikowski S30CR) 10 wt %. La 0.8 Sr 0.2 FeO 3 , 90 wt % c-Al 2 O 3 (Puralox NWa155) Production parameters Spray drying, calcined for 4 h @ 10308C Impregnation, calcined for 2 h @ 11008C BET surface area (m 2 /g) 7.85 47.03