Table 2. Summary of Recently Studied Catalytic Performances of Unsupported, Metal-Supported, Carbon-Based, and Carbon-Supported Catalysts.
catalyst | initial CH4 conversion (%) | reaction temperature (°C) | initial H2 yield mmol/gcat·min | stability (hours) | ref |
---|---|---|---|---|---|
unsupported metal catalysts | |||||
Ni | 25 | 550 | 2.0 | 2 | (54) |
NiO | 575 | 11.7 | 2.5 | (55) | |
Fe | 75 | 900 | 2.75 | 10 | (56) |
Ni–Cu | 85 | 750 | 8 | 5 | (54) |
10% Ni–1% Pd | 57 | 600 | 5.8 | (57) | |
f-Fe65–Al3.7 | 70 | 750 | 4.1 | 6.6 | (58) |
NiCuLa | 79 | 700 | 22 | (59) | |
NiMgAlMo | 36 | 650 | 55 | 0.5 | (60) |
metal/support catalysts | |||||
50% Ni–10% Cu/SiO2 | 83 | 750 | 8.3 | (61) | |
50% Fe/Al2O3 | 45 | 700 | 3 | (62) | |
60% Ni/Al2O3 | 60 | 700 | 6 | (63) | |
9% Co/Al2O3 | 35 | 700 | 7 | (64) | |
40% Fe/MgO | 40 | 700 | 3 | (62) | |
50% Co/MgO | 700 | 7 | (64) | ||
55% Ni/MgO | 75 | 675 | 3.8 | 2.6 | (48) |
50% Fe/TiO2 | 17 | 700 | 3 | (64) | |
55% Ni/2MgO–Al2O3 | 55 | 600 | <6 | (65) | |
9% Ni–1% Co/Al2O3–TiO2 | 72 | 650 | 1 | (66) | |
Co3–xAlxO4 | 44 | 500 | 3.3 | (67) | |
Fe/CeO2 | 54 | 800 | 2.2 | 6 | (68) |
Fe/WO3–ZrO2 | 92 | 800 | 1.8 | 4 | (69) |
Ni–Fe/SiO2 | 59 | 650 | 2.8 | 1 | (70) |
Ni–Fe/MgO | 64 | 700 | 2.6 | 3 | (71) |
Ni/CeO2 | 46 | 550 | 0.08 | 4 | (72) |
carbonaceous catalysts | |||||
carbon black | 85 | 1120 | 2.5 | (73) | |
activated carbon | 67 | 900 | >10 | (74) | |
carbon black | 52 | 900 | >10 | (74) | |
mesoporous carbon | 45 | 900 | >10 | (74) | |
carbon nanofiber | 15 | 900 | >10 | (74) | |
carbon black | 12 | 900 | 0.41 | 2 | (75) |
metal/carbon catalysts | |||||
30% Fe/AC | 18 | 800 | 2.5 | >10 | (76) |
K2CO3/C | 89 | 850 | 0.6 | 10 | (77) |
10% Ni/C (coal char) | 80 | 850 | 10 | 10 | (78) |
8% Ni/C | 55 | 850 | 1.3 | 10 | (79) |
10% Fe/AC | 29 | 850 | 1.1 | 8.3 | (76) |
Fe–Al2O3/AC | 35 | 850 | 5 | (80) | |
Ru/AC | 21 | 800 | 0.26 | 60 | (81) |
Ru/activated biochar | 51 | 800 | 0.23 | 60 | (81) |