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Primary Reforming Catalyst DZC-S169
DZC-S169/DZC-S1614 catalyst is widely used to catalyze the reaction of methane and steam at high temperature and pressure to produce synthesis gas (H2 and CO), which is the most economical method to produce commercial bulk hydrogen used in the industrial synthesis of ammonia and other chemicals.
The reaction is summarized as below:
CH4 + H2O ⇌ CO + 3H2
CO + H2O ⇌ CO2 + H2
PRODUCT DESCRIPTION
Name | Primary Reforming Catalyst | |
Model | DZC-S169 /DZC-S1614 | |
Other names | Steam Methane Reforming (SMR) Catalyst | |
Appearance | 6-hole arc honeycomb | 6-hole arc honeycomb |
Size(mm) | Φ16×9×3.5 | Φ16×14×3.5 |
Bulk density (kg/l) | 0.9±0.1 | 0.9±0.1 |
Crushing strength/(N/CM) | ≥300 | ≥350 |
NiO % | ≥14.0 | ≥14.0 |
SiO₂ % | ≤0.2 | ≤0.2 |
Burning weight loss % | ≤5 | ≤5 |
The catalyst’s sponge micro pore structure can make it better tenacity so that it is of better
heat-expansion & cold-shrink resistance. The 6-holed shape ensures symmetrical stress patterns and no
easy fracture-line.
The reaction normally takes places at outer surface of the catalyst, therefore a uniform nickel coating has
to be insured. The catalyst features an optimized Ni-content, specially adapted to its surface roughness and
porosity. Simultaneously, domed shape allows full utilization of surface.
The catalyst adds rare earth to improve catalyst‘s comprehensive performance. Adding rare earth can
increase catalyst‘s adsorption capacity to water and also improve its activity at low temperature.
Thus this will allow steam/carbon ratio of as low as 2.0 without risk of carbon formation.
In the unlikely event of a plant up-set which does result in carbon formation, the catalyst can be easily
steamed due to large hole sizes, and usually activity can be completely recovered.
Related products
Catalyst for Methanol Production DZC-98-5
Secondary Steam Reforming Catalyst
Ni-Mo Diesel Hydrofining Catalyst (HDS-Y312)
Debenzenizing Catalyst DEB-8
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