Table 4. Ni/Al2O3 Catalysts Reported in the Literature for the Pyrolysis and In-line Steam Reforming of Biomass.
| Catalyst | Feed | Preparation methoda | Reactor configuration | Operating conditionsc | H2 conc. (vol %) | H2 prod. (wt %) | Ref. |
|---|---|---|---|---|---|---|---|
| 20Ni/Al2O3 | pine wood | commercial | fluidized/fixed (1–2 g min–1) | TP = 530–700 °C | 60.0 | 7.2b | Xiao et al.61 |
| TR = 550–710 °C | |||||||
| 20Ni/Al2O3 | pig manure compost | commercial | fluidized/fixed (1–2 g min–1) | TP = 530–700 °C | 56.2 | 5.0b | Xiao et al.61 |
| TR = 550–710 °C | |||||||
| 11Ni/Al2O3 | pine wood sawdust | commercial (G90 LDP) | spouted/fluidized (0.75 g min–1) | TP = 500 °C | 66.0 | 11.2 | Arregi et al.50 |
| TR = 550–700 °C | |||||||
| S/C = 7.7 | |||||||
| 11Ni/Al2O3 | pine wood sawdust | commercial (G90 LDP) | spouted/fixed (0.75 g min–1) | TP = 500 °C | 64.5 | 10.5 | Fernandez et al.98 |
| TR = 600 °C | |||||||
| S/C = 7.7 | |||||||
| 10Ni/Al2O3 | wood sawdust | commercial | fixed/fixed (1 g) | TP = 300–600 °C | 38.1 | 2.2 | Olaleye et al.158 |
| TR = 800 °C | |||||||
| 20Ni/Al2O3 | sewage sludge | commercial | fixed/fixed | TP = 900 °C | 70.0 | 11.6b | Cao et al.156 |
| TR = 400–750 °C | |||||||
| 20Ni/Al2O3 | Japanese cypress | commercial | fixed/fixed (1 g) | T = 450 °C | 35.2 | 5.0b | Kannari et al.159 |
| 12Ni/Al2O3 | cedar wood | iwi | dual fixed bed (0.06 g min–1) | T = 550–650 °C | 60.1 | 8.3 | Miyazawa et al.89 |
| S/C = 0.5 | |||||||
| 20Ni/Al2O3 | wood pellets | iwi | screw-kiln/fixed (4 g min–1) | TP = 500 °C | 44.4 | 2.4 | Efika et al.102 |
| TR = 760 °C | |||||||
| 10Ni/Al2O3 | pine wood sawdust | wi | spouted bed/fluidized (0.75 g min–1) | TP = 500 °C | 64.2 | 10.2 | Santamaria et al.51,100 |
| TR = 600 °C | |||||||
| S/C = 7.7 | |||||||
| 3Ni/Al2O3 | pine sawdust | wi | entrained-flow/fixed (4 g min–1) | TP = 900 °C | 49.3 | 6.1 | Liu et al.160 |
| TR = 800 °C | |||||||
| 15Ni/Al2O3 | cellulose | wi | fixed/fixed (1.5 g) | TP = – | 5.9 | Zou et al.161 | |
| TR = 800 °C | |||||||
| 10Ni/Al2O3 | rice husk | iwi | fixed/fixed (2 g) | TP = 550 °C | 57.6 | 3.7 | Akubo et al.157 |
| TR = 750 °C | |||||||
| 10Ni/Al2O3 | coconut shell | iwi | fixed/fixed (2 g) | TP = 550 °C | 58.2 | 4.4 | Akubo et al.157 |
| TR = 750 °C | |||||||
| 10Ni/Al2O3 | sugar cane | iwi | fixed/fixed (2 g) | TP = 550 °C | 59.2 | 4.6 | Akubo et al.157 |
| TR = 750 °C | |||||||
| 10Ni/Al2O3 | palm kernel shell | iwi | fixed/fixed (2 g) | TP = 550 °C | 57.4 | 5.1 | Akubo et al.157 |
| TR = 750 °C | |||||||
| 10Ni/Al2O3 | cotton stalk | iwi | fixed/fixed (2 g) | TP = 550 °C | 58.0 | 4.1 | Akubo et al.157 |
| TR = 750 °C | |||||||
| 10Ni/Al2O3 | wheat straw | iwi | fixed/fixed (2 g) | TP = 550 °C | 54.1 | 3.3 | Akubo et al.157 |
| TR = 750 °C | |||||||
| 9Ni/Al2O3 | rice husk | wi | drop-tube fixed bed (120 mg) | T = 800 °C | 32.8 | 1.2 | Kuchonthara et al.103 |
| 10Ni/Al2O3 | pine wood | wi | fixed/nonthermal plasma (1 g) | TP = 600 °C | 0.8 | Blanquet et al.162 | |
| TR = 250 °C | |||||||
| steam = 2 g h–1 |
iwi, Incipient wetness impregnation; wi, wetness impregnation.
H2 production defined as gH2/100 gbiomass, daf (dry and ash free).
TP = pyrolysis temperature; TR = reforming temperature.