Research Article
Effect of Operating Conditions on Catalytic Gasification of Bamboo in a Fluidized Bed
Table 2
Comparison with the existing literature.
| Ref | Biomass | C : B | S/B | Agent | ER | (°C) | (% mol) | H2/CO | Gas yield (Nm3/kg) | CCE (%) | H2 | CO |
| This work
| Bamboo | — | — | Air | 0.4 | 400–600 | 6.6–8.16 | 23.5–30.6 | 0.25–0.28 | 1.9–2.0 | 63.6–67.4 | 1 : 1–1 : 1.5 | — | 3.2–9.1 | 21.4–31.7 | 0.1–0.3 | 1.9–2.1 | 59.5–80.1 | — | 1 : 1 | Air-steam | 10.9–16.5 | 36.1–40.3 | 0.3–0.4 | 2.8–2.9 | 87.3–98.5 | [1] | Pine sawdust | 3% | 0.75–0.9 | Air-steam | 0.22–0.3 | 800 | 35.87–40.67 | 22.71–29.88 | 1.2–1.79 | 1.5–2.3 | — | [45] | Rice husk | — | — | Air | 0.25–0.35 | 665–1103 | 4.0–3.3 | 19.9–12.3 | 0.20–0.26 | 1.3–1.9 | 55–81 |
[46] | Sewage sludge | 10, 15% | — | Air | 0.3 | 750–850 | 9.9–15.2 | 6.1–14.4 | 1.05–1.62 | 2.5–2.8 | 69.9–88.6 | 10% | 0.5, 1 | Air-steam | 800 | 15.7–16.8 | 7.5–9.1 | 1.7–2.2 | 2.7–2.8 | 82.5–83.0 | [39] | Pine sawdust | — | 2.81 : 1 | Air-steam | 0.22 | 700–900 | 21.0–38.0 | 33.0–43.0 | 0.5–1.2 | 1.4–2.5 | 78.2–92.6 | | Coir pith | — | — | Air | 0.3–0.5 | 400–900 | 5.6–10.6 | 6.5–12.7 | 0.7–1.0 | 1.9–3.2 | — | [47] | Rice husk | 5.3–8.6 | 9.3–19.6 | 0.4–0.67 | 1.8–2.8 | — | | Saw dust | 5.2–10.1 | 10.78–16.84 | 0.41–0.58 | 2.2–3.7 | — |
[11] | Cellulose | — | — | Air | 0.2 | 600–1000 | 5.29–9.5 | 12.13–23.6 | 0.44–1.46 | 0.3–1.2 | 12.13–23.6 | 0–1.5 | Air-steam | 0.27 | 800 | 13.5–18.6 | 6.4–11.2 | 1.2–2.2 | 0.8–1.0 | — |
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