Modelling oxy-pyrolysis of sewage sludge in a rotary kiln reactor

A mathematical model of a rotary kiln oxy-pyrolyser of sewage sludge is presented. The specific feature of themodel is the consideration of the effect of axial staging of oxygen feeding to the reactor as one important key tothe quality and productivity of the syngas, with a focus on the fate of tar and generation of soot. The gaseousoxidiser is fed to the reactor at multiple locations along its axis in a way that reproduces the paradigm of theZwietering reactor. The fate of gaseous components and tar is followed using a simplified lumped-kinetic mechanismthat was purposely developed. The model implements submodels for heat transfer among the phasesand with the wall which embody radiative, convective and conductive terms. Homogeneous reactions in gasphase are modelled with a kinetic submodel that considers the generation of primary tars from devolatilisation offuel and subsequent formation of secondary tars and soot by thermal cracking. The model validity has beenconfirmed by critical comparison with experimental literature data referring to a similar case. The steady operationof the oxy-pyrolyser is analysed in terms of fluxes of solid fuel and gaseous species, extent of fueldevolatilisation, temperature profiles of solid and gas phases along the reactor. The performance of the reactor ischaracterised in terms of process rate and chemical composition of the produced syngas, along with its heatingvalue and thermal power. The influence of the distributed feeding is assessed by comparison with a benchmarkcase consisting of conventional non-distributed feeding.