Catalysts
C&CS #1050 fluidizable Nickel Steam reforming catalyst
C&CS #1050 is a fluidizable Nickel based steam reforming catalyst, that was developed and scaled-up within the frame of the CE project MEMBER. Its target
Reforming is a process in which hydrocarbons such as natural gas, propane, butane or tars are converted into synthesis gas, which consists mainly of hydrogen (H₂) and carbon monoxide (CO).
Steam Reforming in Chemistry
Steam reforming is a large-scale industrial process for producing synthesis gas from hydrocarbons, such as natural gas (Steam Methane Reforming, SMR). In this process, the CH bonds of the methane molecule (CH₄) and the OH bonds of the water molecule (H₂O) on the surface of a nickel catalyst such as ReforMax® 330 are activated at high temperatures between 700 and 1000 °C. The resulting active species react at the catalyst surface to produce CO and H₂.
Autothermal Reforming
By using oxygen (O₂) instead of steam, a nickel catalyst such as ReforMax® 330 can also be used in autothermal reforming. In this process, naphtha can be converted to synthesis gas with steam instead of natural gas, using a pre-reforming catalyst such as ReforMax® 100. In ammonia plants, the synthesis gas obtained after steam reforming is converted to N₂-containing synthesis gas with additional air in a secondary reforming process using the ReforMax® 410 catalyst.
Endogas in steel production
In the steel industry, a nitrogen-containing synthesis gas, known as endogas, is produced for surface hardening of steel. This occurs through the partial oxidation of natural gas with air and the catalyst ReforMax® 117 in endogas generators of heat treatment furnaces. If the air-to-natural gas ratio is increased, an exothermically produced gas, called exogas, is generated with the same catalyst in the substoichiometric range.
Hydrogen Production
Hydrogen is typically produced by steam reforming of natural gas followed by CO conversion of the synthesis gas. In locations without access to natural gas, hydrogen can alternatively be produced by steam reforming of methanol using the ReforMax® M catalyst.
Innovations
A promising alternative to conventional hydrogen production from natural gas is the so-called sorption-enhanced reforming process. This process uses the fluidizable steam reforming catalyst C&CS #1050 in combination with a CO₂ adsorbent to produce hydrogen – with significantly reduced CO₂ emissions.
C&CS #1050 is a fluidizable Nickel based steam reforming catalyst, that was developed and scaled-up within the frame of the CE project MEMBER. Its target
C&CS #1050 B is a novel nickel-based tar reforming catalyst developed based on the catalyst technology developed in the EU project MEMBER for the Sorption
ReforMax® 450 LDP is an aluminum oxide-supported nickel catalyst in the form of ribbed rings for the steam reforming of hydrocarbons to produce a mixture
ReforMax® 117 RR is a nickel-based catalyst for the dissociation of ammonia in exhaust gases. The catalyst’s ribbed rings ensure high stability and protect it
ReforMax® M is a copper catalyst on a zinc oxide/aluminum oxide support in tablet form, used in methanol steam reforming (MeOH reforming) for hydrogen production.
ReforMax 210 is an alkali-doped nickel catalyst supported on ten-hole rings for the steam reforming of e.g. LPG-containing feed streams (primary reforming) for the production
C&CS #1300 is a tablet-form glycerol vapor reforming catalyst developed for the production of synthesis gas from waste glycerol from biodiesel production. The goal of
The C&CS #592 is a copper catalyst in tablet form that primarily functions as an catalyst for oxygen removal. It is most commonly used in
ReforMax® 117 RR, our best-selling endogas catalyst, is a catalyst consisting of finely dispersed nickel on basic magnesium oxide – resulting in low coking. It
High-performance catalyst for steam reforming in ammonia, hydrogen, and methanol production. ReforMax® 210 LDP is a potassium-doped, nickel-based catalyst for natural gas and liquefied petroleum
