“…Detailed description of the model, balance equations and equilibrium modifications, are presented in author's previous study [15]. The following assumptions were applied to perform following calculations: gasification reactor is assumed to be a moving bed reactor, fed from the top, waste feed is 1000 kg/h, the basic amount of air fed into the reactor is calculated based on equivalence ratio typical for biomass gasification [16,17] ER=0.25, enriched air is assumed to contain up to 35% of oxygen, nitrogen from air and inorganic substance from is treated as inert and does not influence chemistry of the process, heat loss of the system is estimated to be equal to 15% of physical enthalpy of products. The reactor itself can be divided into 3 zones: drying, gasification and ash melting.…”