Tubular Reforming Catalyst for Feedstocks Heavy Natural Gas to LPG and for Operation Under High Heat Flux Conditions
Tubular Reforming Catalyst
Hydrocarbon First-stage Conversion Catalyst
The catalyst is suitable for the first conversion section of the synthesis ammonia, methanol or hydrogen production plant from
different raw materials such as natural gas, coke oven gas, refinery gas, naphtha, and oilfield associated gas, to convert
hydrocarbons and water into H₂, CO, CO₂ Reaction. It is also suitable for ammonia cracking hydrogen production plant.
Conditions of Use
Inlet temperature 400-600℃ ; output temperature 650-850℃
Water to carbon ratio:2.5-5.0
Carbon space velocity:600-2000h⁻¹
Sulfur content in feed gas≤0.2×10⁻⁶
Bulk density (kg/l)
Average strength before compression (lateral compression) (N/cm)
Burning weight loss %
Activity at 800℃ (dry gas CH₄) V %: ≤21 (Z118Y superior product)
Activity at 520℃ (dry gas CH₄) V %: ≤64 (Z118Y-1 superior product)
Packaging, Storage and Shipping
Sealed iron drum packaging(50±0.2kg/Barrel).
It must be moisture-proof, drop-proof and anti-rolling during transportation.
Store in a ventilated and dry room. Products with damaged packaging and unclear labels cannot be used.