Table 14. Bimetallic Catalysts Reported in the Literature for Biomass Pyrolysis and In-line Steam Reforming.
| Catalyst | Feed | Preparation methodb | Reactor configuration | Operating conditionsc | H2 conc. (vol %) | H2 prod. (wt %) | Ref. |
|---|---|---|---|---|---|---|---|
| 5Ni5Co/Al2O3 | pinewood sawdust | wi | spouted/fluidized (0.75 g min–1) | TP = 500 °C | 63.4 | 9.8 | Santamaria et al.199 |
| TR = 600 °C | |||||||
| S/C = 7.7 | |||||||
| 7.5Ni2.5Co/Al2O3 | pinewood sawdust | wi | spouted/fluidized (0.75 g min–1) | TP = 500 °C | 63.6 | 9.9 | Santamaria et al.199 |
| TR = 600 °C | |||||||
| S/C = 7.7 | |||||||
| Ni-Fe/Al2O3 | cedar wood | cp | dual fixed (0.06 g min–1) | T = 550 °C | 50.6 | 5.2 | Wang et al.201 |
| S/C = 0.57 | |||||||
| Co-Fe/Al2O3 | cedar wood | cp | dual fixed (0.06 g min–1) | T = 600 °C | 50.3 | 6.0 | Wang et al.202 |
| S/C = 0.57 | |||||||
| Ni-Cu/MgO-Al2O3 | cedar wood | cp | dual fixed (0.06 g min–1) | T = 650 °C | 55.2 | 8.3 | Li et al.87 |
| S/C = 0.38 | |||||||
| 0.1Pt-4Ni/CeO2-Al2O3 | cedar wood | wi | dual fixed (0.06 g min–1) | T = 550 °C | 54.1 | 6.1 | Nishikawa et al.203 |
| 0.1Rh-4Ni/CeO2-Al2O3 | cedar wood | wi | dual fixed (0.06 g min–1) | T = 550 °C | 48.0 | 4.6 | Nishikawa et al.203 |
| 0.5Ru-4Ni/CeO2-Al2O3 | cedar wood | wi | dual fixed (0.06 g min–1) | T = 550 °C | 47.4 | 4.5 | Nishikawa et al.203 |
| Ni-Fe/RHAa | rice husk | iwi | fixed/fixed | TP = 800 °C | 31.5 | 5.5 | Shen et al.185 |
| TR = 600–900 °C | |||||||
| Ni-Fe/RHCa | rice husk | iwi | fixed/fixed | TP = 800 °C | 22.7 | 4.3 | Shen et al.185 |
| TR = 600–900 °C |
RHA, Rice husk ash; RHC, rice husk char.
iwi, Incipient wetness impregnation; wi, wet impregnation; cp, co-precipitation.
TP = Pyrolysis temperature; TR = reforming temperature.