Table 3 Non-condensable gas yield (mmol/g biomass) of various catalytic thermochemical treatment processes using different biomass feedstocks
From: Sustainable co-production of porous graphitic carbon and synthesis gas from biomass resources
Carbon source (process) | Catalyst or co-reactants | Synthesis temperature | H2 | CO | CO2 | CH4 | Reference |
|---|---|---|---|---|---|---|---|
Corncobs | Limonite | 750 °C | 21.7 | 12.5 | 2.9 | 3.7 | Zhao et al.80 |
Corncobs | Ni/Al2O3 | 750 °C | 25.4 | 13.5 | 5.2 | 2.8 | Zhao et al.80 |
Pine wood | K2CO3 | 700 °C | 4.0 | 2.6 | 3.6 | 0.6 | Fan et al.81 |
Seaweed (ATT) | Ni/ZrO2, Steam, NaOH | 500 °C | 69.69 | 0.2 | 0.2 | 2.5 | Zhang et al.41 |
Pine wood | Ni/Iron Slag | 900 °C | 23.2 | 27.3 | 0.6 | 4.2 | Liu et al.82 |
Pine wood | Ni/Al2O3 | 900 °C | 24.9 | 30.6 | 0.5 | 1.2 | Liu et al.82 |
Wood waste | – | 900 °C | 9.9 | 9.8 | 5.3 | 1.4 | Present work |
Wood waste (2-step graphitization) | KOH | 400 °C + 900 °C | 7.5 | 11.5 | 4.8 | 0.4 | Present work |
Wood waste (ATG) | KOH, Ni/ZrO2 | 900 °C | 21.1 | 23.5 | 6.8 | 0.7 | Present work |
