Catalyst contains Fe2O3 and FeO as main components, and K2O, Al2O3, MgO, CaO as promoters. An active component of the catalyst after its reduction is iron. Alumina is structural promoter which provides the catalyst with a good thermal stability and a high mechanical strength. Calcium oxide and magnesium oxide increase resistances of the catalyst to overheating and to poisoning by sulfur and chlorine compounds. Potassium oxide is an promoter which enhances activity of the catalyst.

The RANG-19 and RANG-19 PR catalysts are designed for the methanation of carbon monoxide and carbon dioxide. This process allows a practically full removal of carbon oxides from gas streams and is used mainly in the plants producing the synthesis gas for the ammonia production.

The TMC-3/1, TMC-3/1-K, and TMC-3/1-KC catalysts are designed for the low-temperature shift conversion in the process of hydrogen and ammonia synthesis gas production.

The TZC-3/1 catalyst is designed for the high temperature shift conversion in the process of hydrogen and ammonia synthesis gas production.

The G-0110, G-0110-7H, G-0110-7H/C and G-0105-7H/C catalysts are designed for secondary reforming of natural gas. The process of the secondary reforming proceeds in the presence of air and/or oxygen, depending on the designation of the synthesis gas thus produced. The catalysts are also designed for the partial oxidation of natural gas with oxygen or air, in the presence of steam and/or carbon dioxide.

The G-0117, G-0117-7H, G-0117-7H/C and G-0117 K-7H/C catalysts are designed for the primary steam reforming of natural gas to convert it to hydrogen or the synthesis gas for the production of ammonia, methanol, and other chemical products obtained from hydrogen and carbon oxides. The catalysts are used to tubular primary reforming.

The PSC zinc sorbent is designed for the removal of hydrogen sulfide and reactive organic sulfur compounds such as mercaptans and bisulfides from the natural gas, refinery gas, naphta, and other hydrocarbon feedstocks used for the manufacture of hydrogen and the synthesis gases in ammonia and methanol production plants. The PSC sorbent is applied in the desulfurization system separately or along with a hydrogenation catalyst used for the conversion of stable compounds of sulfur to hydrocarbons and hydrogen sulfide.

High-alumina balls can be used in catalytic reactors as an underlay or upper safe-guard layer of catalytic bed. They can also be used as an inert packing of dead spaces in the reactors. Considering their remarkably high mechanical strength, abrasion resistance, stability to heat, and chemical resistance, the high-alumina balls can be applied in many processes of various branches of chemical industry.