Abstract

In this study, the influence of potassic additives (K2CO3 and biomass ash (BA)) on sludge gasification under model flue gases was investigated. Two model gases consisting of O2/CO2/N2 and O2/CO2/H2O/N2 were used as gasifying agents. Under O2/CO2/N2 atmosphere, the lower heating values (LHV) of produced gas were in a range of 3.07–3.79 MJ/Nm3, and cold gas efficiency (CGE) were in a range of 47–66%. When steam was introduced into the gasification atmosphere, the efficiency of the process significantly improved. LHV of the produced gas under O2/CO2/H2O/N2 atmosphere was in a range of 6.48–7.18 MJ/Nm3, and CGE was in a range of 73–88%. K2CO3 had an obvious catalytic effect on sludge gasification process. Additionally, K2CO3 had stronger catalytic effect under steam-free atmosphere and it was better in promoting CO generation when compared with BA. BA exhibited the ability to increase gas yield under steam-free atmosphere, while it only had a slight effect under steam-containing atmosphere. Based on continuous monitoring of gas during gasification process, LHV of the produced gas could be increased by nearly twofold, possibly up to 11.96 MJ/Nm3, by controlling the proper reaction time (10–12 min) to prevent the dilution effect from excessive gasifying agents.

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