Solar-driven biomass chemical looping gasification using Fe3O4 for syngas and high-purity hydrogen production

• Published in: Chemical engineering journal (Lausanne, Switzerland : 1996) Switzerland : 1996), 2024-01, Vol.479, p.147901, Article 147901
• Main Authors: Xu, Dequan, Wang, Bo, Li, Xian, Cheng, Yoke Wang, Fu, Wenming, Dai, Yanjun, Wang, Chi-Hwa
• Format: Article
• Language: English
• Subjects: Biomass; Chemical looping gasification; Hydrogen; Solar energy; Syngas
• ISSN: 1385-8947; 1873-3212
• DOI: 10.1016/j.cej.2023.147901

[Display omitted] •A novel solar-driven biomass chemical looping gasification system is studied.•The system achieves a carbon-gas yield of 0.69 and an energy upgrade factor of 0.71.•The fuel reactor produced CH4, CO, CO2 and H2 at 0.63, 11.86, 8.85, and 18.53 mmol/g.•High-purity H2 is produced at 7.17 mmol/g in a separated stream.•Fayalite is found as a byproduct due to the interaction between reactants. A novel solar-driven biomass chemical looping gasification (SBCLG) system was proposed and experimentally demonstrated for the co-production of pure hydrogen and syngas from biomass wastes using high-flux solar irradiation. In this system, a steam reactor and a solar fuel reactor were adopted to replace the air and fuel reactors in a typical biomass chemical looping gasification (BCLG) system, respectively. The SBCLG exhibits two advantages over BCLG: (1) the syngas yield is raised as the high-temperature process heat is provided by solar radiation rather than biomass combustion, and (2) a pure hydrogen stream is generated in addition to the syngas stream, which allows a flexible adjustment of the carbon-to-hydrogen ratio for downstream chemical processes. This study marked the first demonstration of a complete cycle of SBCLG in a cavity-type packed-bed solar reactor under simulated high-flux solar irradiation. Magnetite (Fe3O4) was circulated between the steam reactor and the solar fuel reactor as the oxygen carrier (OC). The optimal operational parameters, the reaction temperature and solid contact pattern, were first determined in preliminary experiments in an electric furnace. Then, the effect of biomass to oxygen carrier mass ratio (mRH:mOC) on the key performance indicators was also investigated in a solar reactor. When mRH:mOC = 1:2, the highest values of the average carbon-gas yield of 0.69 ± 0.05 and energy upgrade factor of 0.71 ± 0.04 were achieved. The solar fuel reactor produced CH4, CO, CO2 and H2 at 0.63, 11.86, 8.85, and 18.53 mmol/g biomass, respectively, with the steam reactor yielding high-purity H2 at 7.17 mmol/g biomass. The results indicated that the SBCLG is a viable method for co-production of pure hydrogen and syngas in separate streams.