Table 7. Ni/Metal Oxide Supported Catalysts Reported in the Literature for the Pyrolysis and In-line Steam Reforming of Biomass and Plastic Wastes.
| Catalyst | Feed | Preparation methoda | Reactor configuration | Operating conditionsb | H2 conc. (vol %) | H2 prod. (wt %) | Ref. |
|---|---|---|---|---|---|---|---|
| 20Ni/SiO2 | wood pellets | iwi | screw-kiln/fixed (4 g min–1) | TP = 500 °C | 38.7 | 2.0 | Efika et al.102 |
| TR = 760 °C | |||||||
| 20Ni/SiO2 | wood pellets | sg | screw-kiln/fixed (4 g min–1) | TP = 500 °C | 37.6 | 2.0 | Efika et al.102 |
| TR = 760 °C | |||||||
| 10Ni/SiO2 | pine wood sawdust | wi | spouted/fluidized (0.75 g min–1) | TP = 500 °C | 55.7 | 1.6 | Santamaria et al.51,100 |
| TR = 600 °C | |||||||
| S/C = 7.7 | |||||||
| 12Ni/MgO | cedar wood | iwi | dual fixed bed (0.06 g min–1) | T = 550–650 °C | 32.4 | 2.3 | Miyazawa et al.89 |
| S/C = 0.5 | |||||||
| 6Ni/MgO | cotton stalk | commercial | bubbling fluidized/entrained flow/fixed (3.3 g min–1) | TP = 600 °C | 38.0 | 6.5 | Chen et al.170 |
| TG = 800 °C | |||||||
| TR = 850 °C | |||||||
| S/B = 1–4 | |||||||
| 6Ni/MgO | timber wood sawdust | commercial | bubbling fluidized/entrained flow/fixed | TP = 600 °C | 51.0 | 7.6 | Ma et al.169 |
| TG = 700–850 °C | |||||||
| TR = 700–850 °C | |||||||
| S/B = 3 | |||||||
| 10Ni/MgO | pine wood sawdust | wi | spouted/fluidized (0.75 g min–1) | TP = 500 °C | 61.6 | 9.1 | Santamaria et al.51,100 |
| TR = 600 °C | |||||||
| S/C = 7.7 | |||||||
| 12Ni/TiO2 | cedar wood | iwi | dual fixed bed (0.06 g min–1) | T = 550–650 °C | 57.4 | 8.2 | Miyazawa et al.89 |
| S/C = 0.5 | |||||||
| 10Ni/TiO2 | pine wood sawdust | wi | spouted/fluidized (0.75 g min–1) | TP = 500 °C | 57.9 | 7.2 | Santamaria et al.51,100 |
| TR = 600 °C | |||||||
| S/C = 7.7 | |||||||
| 12Ni/ZrO2 | cedar wood | iwi | dual fixed bed (0.06 g min–1) | T = 550–650 °C | 52.7 | 6.6 | Miyazawa et al.89 |
| S/C = 0.5 | |||||||
| 10Ni/ZrO2 | pine wood sawdust | wi | spouted/fluidized (0.75 g min–1) | TP = 500 °C | 65.4 | 10.7 | Santamaria et al.40,51,100 |
| TR = 600 °C | |||||||
| S/C = 7.7 | |||||||
| 12Ni/CeO2 | cedar wood | iwi | dual fixed bed (0.06 g min–1) | T = 550–650 °C | 51.9 | 5.9 | Miyazawa et al.89 |
| S/C = 0.5 | |||||||
| 10Ni/MgO | PP | wi | fixed/fixed (1 g) | TP = 500 °C | 32.6 | 3.0 | Wu and Williams164 |
| TR = 800 °C | |||||||
| steam = 4.74 g h–1 | |||||||
| 10Ni/MgO | LDPE | wi | fixed/fixed (2 g) | TP = 500 °C | 48.8 | 7.4 | Huang et al.171 |
| TR = 800 °C | |||||||
| S/P = 2 | |||||||
| 10Ni/CeO2 | PP | wi | fixed/fixed (1 g) | TP = 500 °C | 75.5 | 11.6 | Wu and Williams164 |
| TR = 800 °C | |||||||
| steam = 4.74 g h–1 | |||||||
| 10Ni/CeO2 | LDPE | wi | fixed/fixed (2 g) | TP = 500 °C | 57.2 | 12.2 | Huang et al.171 |
| TR = 800 °C | |||||||
| S/P = 2 | |||||||
| 20Ni/ZrO2 | PS | cp | fixed/fixed (0.3 g) | TP = 500 °C | 58.0 | 10.0 | Zhou et al.172 |
| TR = 500 °C | |||||||
| steam = 0.02 mL min1 | |||||||
| 10Ni/Y2O3 | LDPE | wi | fixed/fixed (2 g) | TP = 500 °C | 53.1 | 9.8 | Huang et al.171 |
| TR = 800 °C | |||||||
| S/P = 2 |
iwi, Incipient wetness impregnation; wi, wet impregnation; cp, co-precipitation; sg, sol–gel.
TP = Pyrolysis temperature; TR = reforming temperature; TG = gasification temperature.