Gasification is a thermochemical process that converts different solid fuels into a synthetic gas (syngas) that can be utilized for different purposes. The possibility to gasify different kind of waste, as alternative to the traditional combustion processes, is attractive for several reasons, by way of an example the small scale of plants and the related social acceptability can be cited. Main constraint to a wide utilization of gasification is the parallel and undesired production of by-products that are mainly constituted by heavy hydrocarbons condensable at ambient temperature (tar) and carbonaceous particle fines. This work is conceptually divided into two parts: a description of the main reaction pathways occurring in a bubbling fluidized bed reactor operated as gasifier (BFBG) with the aim to highlight what is the pathway (and the reactor zone) that favors the heavy hydrocarbons formation; a discussion about experimental results obtained by operating a pre-pilot BFB gasifier under different operating conditions with the aim to reduce the formation of heavy hydrocarbons. The experimental tests have been carried out by feeding polyethylene in a BFB gasifier and by injecting the air stream, utilized as gasifying agent, in different positions: (a) at bed bottom (indicated also as primary zone) without any splitting of the flow rate; (b) at bed bottom and in the splashing zone, that is the volume just above primary zone, by splitting into two streams the necessary air flow rate; (c) at bed bottom, in the splashing zone and in the freeboard region, by splitting into three streams the air flow rate. Results indicate that staging of air stream can be a valid method to impede or reduce the formation of condensable compounds provided that air is well distributed in order to avoid segregation, the injection is made in the zone were heavy stable hydrocarbons are not yet formed and the splitting rates between primary and secondary streams is accurately calculated. (C) 2012 Elsevier Ltd. All rights reserved.