Özet
Sewage sludges were evaluated for hydrogen production by catalytic gasification in a fixed bed reactor under various gasifying agents, including CO2, air, steam, steam-air and steam-CO2 mixtures in order to improve the gasification efficiency. Catalytically active minerals, dolomite, olivine and limonite, have brought obvious improvements by a complete carbon conversion. The best results regarding the carbon conversion of 88% were obtained in steam-air gasification whereas carbon conversion exceeded 99% in the presence of catalytic minerals. The low calorific value of the char samples in 0.1–0.2 MJ/kg and high syngas yields of 15.4–17.0% in total upon catalytic gasification supported the improved efficiencies in comparison to the noncatalytic situation with 1.9 MJ/kg and 14.4%, respectively. CH4 and C2–C5 compounds in the product gas have been reduced in the presence of catalytic minerals as an indication of the increased tar reforming activity favoring hydrogen production. GC-MS measurements of tar samples for steam-air gasification have confirmed the catalytic influence of these minerals on tar reduction via the ring-opening reactions or dealkylation reactions. All these effects were more pronounced in the presence of limonite as the optimal natural mineral for hydrogen production.
| Orijinal dil | İngilizce |
|---|---|
| Sayfa (başlangıç-bitiş) | 966-980 |
| Sayfa sayısı | 15 |
| Dergi | International Journal of Hydrogen Energy |
| Hacim | 142 |
| DOI'lar | |
| Yayın durumu | Yayınlandı - 27 Haz 2025 |
Bibliyografik not
Publisher Copyright:© 2025 Hydrogen Energy Publications LLC
BM SKH
Bu sonuç, aşağıdaki Sürdürülebilir Kalkınma Hedefine/Hedeflerine katkıda bulunur
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SKH 7 Erişilebilir ve Temiz Enerji
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SKH 13 İklim Eylemi
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