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This study presents a novel method for continuous high-purity hydrogen production from glycerol using enhanced-sorption chemical looping steam reforming in moving-bed reactors. The low-cost NiO/NiAl2O4 catalyst effectively converts glycerol and steam to hydrogen with over 90% purity at temperatures of 500–600 °C and steam to carbon ratios of 1.5–3.0, while simultaneously capturing CO2. The process integrates oxidation, steam reforming, water gas shift reaction, and CO2 removal in a single reactor, achieving
- Author
- Arthur Freitas
- Language
- EN