Abstract
Catalytic gasification of cellulose was carried out in a U-type fixed reactor with Ni loaded MSU-F catalyst (Ni/MSU-F) and Ni loaded γ-Al2O3 (Ni/γ-Al2O3). The characteristics of the catalysts were analyzed by using X-ray diffraction, H2-temperature programmed reduction, and Brunauer-Emmett-Teller analyses. The operation conditions of catalytic gasification reactions were 750°C and 0.2 equivalence ratio. Air was used as gasification agent. Catalytic gasification characteristics, such as gas yield and gas composition (H2, CO, CO2, C1-C4), were measured and calculated. The gas yield of Ni/MSU-F was much higher than that of Ni/γ-Al2O3. Especially high amount of hydrogen was produced by Ni/MSU-F.
Original language | English |
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Pages (from-to) | 3205-3208 |
Number of pages | 4 |
Journal | Bulletin of the Korean Chemical Society |
Volume | 35 |
Issue number | 11 |
DOIs | |
State | Published - 20 Nov 2014 |
Keywords
- Air gasification
- Cellulose
- H
- Ni/MSU-F