Physicochemical Properties
| Catalyst | AM-2-412Q | AM-2-413Q |
| Form | Four-hole convex cylindrical | Four-hole convex cylindrical |
| Length | 8-10 | 15-17 |
| Outer diameter | 16 | 16 |
| Inner diameter | 4X4 | 4x4 |
| Bulk density | 0.9-1.05 | 0.9-1.05 |
| Radial crushing strength | >=200 | >=300 |
| Active component | 13+1% | 13+1% |
| Loading position | Upper half of the reformer tube | Lower half of the reformer tube |
AM-2-301/AM-2-302 steam reforming catalysts are suitable for the steam reforming process of producing hydrogen the synthesis gas, and synthesis gas from various refinery dry gas, etc.
AM-2-301steam reforming catalyst is installed in the upper half of the reformer tube, and AM-2-302 steam reforming catalyst is installed in the lower half of the reformer tube.
AM-2-301/AM-2-302 steam reforming catalysts have the characteristics of a large geometric surface, low bulk density, good heat transfer effect, high catalyst activity, low bed resistance, and high operating flexibility.
| Catalyst | AM-2-301 | AM-2-302 |
| Form | Light black Four-hole convex cylindrical | Gray-green Four-hole convex cylindrical |
| Length | 8-10 | 15-17 |
| Outer diameter | 16 | 16 |
| Inner diameter | 4X4 | 4x4 |
| Bulk density | 0.9-1.15 | 0.9-1.15 |
| Radial crushing strength | >=200 | >=300 |
| Active component | NiO>=16 | NiO>=10 |
| Active Agent | K2O>=2 | |
| Loading position | Upper half of the reformer tube | The lower half of the reformer tube |