Table 5. Ni/Al2O3 Catalysts Reported in the Literature for the Pyrolysis and In-line Steam Reforming of Plastic Wastes.
| Catalys | Feed | Preparation methoda | Reactor configuration | Operating conditionsb | H2 conc. (vol %) | H2 prod. (wt %) | Ref. |
|---|---|---|---|---|---|---|---|
| Ni/Al2O3 | PP | commercial C11-NK | fluidized/fluidized (1 g min–1) | TP = 600 °C | 70.0 | 34.0 | Czernik and French54 |
| TR = 850 °C | |||||||
| S/C = 4.6 | |||||||
| 11Ni/Al2O3 | HDPE | commercial (G90 LDP) | spouted/fixed (0.75 g min–1) | TP = 500 °C | 71.0 | 34.5 | Erkiaga et al.97 |
| TR = 700 °C | |||||||
| S/C = 3.1 | |||||||
| 11Ni/Al2O3 | HDPE | commercial (G90 LDP) | spouted/fluidized (0.6 g min–1) | TP = 500 °C | 72.7 | 38.1 | Barbarias et al.44 |
| TR = 700 °C | |||||||
| S/C = 3.9 | |||||||
| 11Ni/Al2O3 | HDPE | commercial (G90 LDP) | spouted/fluidized (0.75 g min–1) | TP = 500 °C | 69.8 | 37.3 | Barbarias et al.56,99 |
| TR = 700 °C | |||||||
| S/C = 3.1 | |||||||
| 11Ni/Al2O3 | PP | commercial (G90 LDP) | spouted/fluidized (0.75 g min–1) | TP = 500 °C | 70.1 | 34.8 | Barbarias et al.56 |
| TR = 700 °C | |||||||
| S/C = 3.1 | |||||||
| 11Ni/Al2O3 | PS | commercial (G90 LDP) | spouted/fluidized (0.75 g min–1) | TP = 500 °C | 65.4 | 29.1 | Barbarias et al.46,56 |
| TR = 700 °C | |||||||
| S/C = 2.9 | |||||||
| 11Ni/Al2O3 | PET | commercial (G90 LDP) | spouted/fluidized (0.75 g min–1) | TP = 500 °C | 63.6 | 18.2 | Barbarias et al.56 |
| TR = 700 °C | |||||||
| S/C = 4.3 | |||||||
| 11Ni/Al2O3 | HDPE 48 wt %; PP, 35 wt %; PS, 9 wt %; PET: 8 wt % | commercial (G90 LDP) | spouted/fluidized (0.75 g min–1) | TP = 500 °C | 63.9 | 32.5 | Barbarias et al.56 |
| TR = 700 °C | |||||||
| S/C = 3.2 | |||||||
| 10Ni/Al2O3 | PP | wi | spouted/fluidized (0.75 g min–1) | TP = 500 °C | 70.8 | 34.1 | Arregi et al.55 |
| TR = 700 °C | |||||||
| S/C = 3.1 | |||||||
| Ni/Al2O3 (1:1 molar ratio) | PP | cp | fixed/fixed (1 g) | TP = 500 °C | 66.6 | 24.8 | Wu and Williams150 |
| TR = 800 °C | |||||||
| steam = 4.74 g h–1 | |||||||
| 10Ni/Al2O3 | PP | wi | fixed/fixed (1 g) | TP = 500 °C | 56.3 | 11.5 | Wu and Williams164 |
| TR = 800 °C | |||||||
| steam = 4.74 g h–1 | |||||||
| 10Ni/Al2O3 | PE | wi | fixed/nonthermal plasma (1 g) | TP = 500 °C | 0.9 | Aminu et al.165 | |
| TR = 250 °C | |||||||
| steam = 4 g h–1 | |||||||
| 10Ni/Al2O3 | HDPE | wi, cp, sg | fixed/fixed (1 g) | TP = 500 °C | 62.0 | 12.1 | Yao et al.63 |
| TR = 800 °C | |||||||
| steam = 6 g h–1 | |||||||
| 10Ni/Al2O3 | PP | wi, cp, sg | fixed/fixed (1 g) | TP = 500 °C | 59.4 | 13.4 | Yao et al.63 |
| TR = 800 °C | |||||||
| steam = 6 g h–1 | |||||||
| 10Ni/Al2O3 | PS | wi, cp, sg | fixed/fixed (1 g) | TP = 500 °C | 57.9 | 12.5 | Yao et al.63 |
| TR = 800 °C | |||||||
| steam = 6 g h–1 | |||||||
| 5 Ni/Al2O3 | PP | wi | fixed/fixed (1 g) | TP = 500 °C | 49.5 | 6.9 | Acomb et al.163 |
| TR = 800 °C | |||||||
| steam = 4.74 g h–1 | |||||||
| 5 Ni/Al2O3 | LDPE | wi | fixed/fixed (1 g) | TP = 500 °C | 53.1 | 9.2 | Acomb et al.163 |
| TR = 800 °C | |||||||
| steam = 4.74 g h–1 | |||||||
| 5 Ni/Al2O3 | PS | wi | fixed/fixed (1 g) | TP = 500 °C | 60.0 | 7.4 | Acomb et al.163 |
| TR = 800 °C | |||||||
| steam = 4.74 g h–1 |
wi, Wetness impregnation; cp, co-precipitation; sg, sol–gel; ie, ion-exchange.
TP = Pyrolysis temperature; TR = reforming temperature.