4.7 Article

Study on characteristics, hydrogen-rich gas, bio-oil production, and process optimization of co-pyrolysis of sewage sludge and wheat straw

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DOI: 10.1016/j.csite.2023.102888

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Sewage sludge; Co-pyrolysis; Synergy; Bio-oil; Response surface method; Hydrogen

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This research investigates the co-pyrolysis of sewage sludge and wheat straw. The effects of mix ratio and interactions between SS and WS were studied using TG and fixed bed. The mix ratio, N2 flow rate, and pyrolysis temperature were examined for fixed bed pyrolysis, and the response surface method was applied to optimize the process. Increasing the WS ratio reduces pyrolysis residual rate, and there were substantial interactions between 200 and 400 degrees during co-pyrolysis. The syngas and bio-oil yields in fixed bed pyrolysis were mainly affected by N2 flow rate and pyrolysis temperature.
Sewage sludge (SS) and wheat straw (WS) are wastes that need to be treated urgently. In this research, the co-pyrolysis of SS and WS was investigated utilizing a thermogravimetric analyzer (TG) and a fixed bed. Using the Coats-Redfern approach, the effects of the mix ratio and the interactions of the SS and WS were investigated, and the effects of mix ratio, N2 flow rate, and pyrolysis temperature were examined for fixed bed pyrolysis. The response surface method (RSM) was applied in fixed bed pyrolysis to optimize the process. Increasing WS ratio can reduce py-rolysis residual rate to 23.8% for TG analysis. The reaction activation energy (E) increased with WS ratio. For the co-pyrolysis, there were substantial interactions between 200 and 400 degrees. For fixed bed pyrolysis, syngas and bio-oil yields were mainly affected by N2 flow rate and pyrolysis temperature. The components with the highest amount in bio-oil gradually changed from

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