Table 18. Catalytic Fast Pyrolysis of Furfural (FF) to Aromaticsa.
Aromatics
distribution (selectivity) (%) |
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Entry | Feed | Catalyst (Si/Al ratio) | GHSV (h–1) | Carrier gas | Pfurfural (Torr) | T (°C) | TOS (min) | Conv. (%) | Aromatics Sel. (%) | Aromatics carbon yield (%) | Benzene | Toluene | Xylene | Ref |
1 | FF | 0.5 wt% Zn/ H-ZSM-5 (40) | 2412 | air | 5.6 | 500 | 13 | 100 | 20.7 | 20.7 | 70.5 | 26.5 | 0 | (279) |
2 | FF | 1.5 wt% Zn/ H-ZSM-5 (40) | 2412 | air | 5.6 | 500 | 13 | 100 | 26.3 | 26.3 | 71.6 | 25.0 | 0 | (279) |
3 | FF | H-ZSM-5 (23) | 0.5b | N2d | – | 500 | – | 100 wt | 50.3 wt | 50.3 wt | 10.0 | 16.8 | 19.6 | (281) |
4 | FF | 0.3 H-ZSM-5 (23)c | 0.5b | N2d | – | 500 | – | 100 wt | 34.4 wt | 34.4 wt | 10.2 | 14.1 | 16.5 | (281) |
5 | FF | 0.5 H-ZSM-5 (23)c | 0.5b | N2d | – | 500 | – | 100 wt | 35.2 wt | 35.2 wt | 16.1 | 7.4 | 22.8 | (281) |
6 | FF | 0.7 H-ZSM-5 (23)c | 0.5b | N2d | – | 500 | – | 100 wt | 45.9 wt | 45. 9 wt | 12.6 | 17.7 | 20.7 | (281) |
7 | FF | 0.9 H-ZSM-5 (23)c | 0.5b | N2d | – | 500 | – | 100 wt | 53.9 wt | 53.9 wt | 23.6 | 20.6 | 16.8 | (281) |
8 | FF | 1.1 H-ZSM-5 (23)c | 0.5b | N2d | – | 500 | – | 100 wt | 45.7 wt | 45.7 wt | 18.6 | 22.8 | 18.9 | (281) |
9 | FF | 0.5 wt% Mg–1 wt% Cu/BEA (100) | 1.2f | Ar | – | 700–750 | 60 | 100 | ∼45 | ∼45 | 100 | 0 | 0 | (282) |
10 | FF | H-ZSM-5 (15)e | – | He | – | 300, 600 | – | – | – | 35.1 | 24.2 | 30.2 | 8.7 | (23) |
11 | HMF | H-ZSM-5e | – | He | – | 300, 600 | – | – | – | 25.5 | 24.8 | 29.9 | 11.5 | (23) |
Products were analyzed by GC and GC-MS (FID).
Feeding rate (mL/h).
Pretreated with HCl (the number in front indicates the concentration).
N2 (10 mL/min).
In a tandem microreactor.
WHSV.