Catalyst of ammonia synthesis is designed for the operation under the temperature from 400 °С till 600 °С and under the pressure from 15 till 55 МРа. It is produced in two grades: SA-S (oxidize) and SA-SV (deoxidized).

It is designed for steam, steam carbon-dioxide and air reforming of gaseous hydrocarbons under normal pressure and tension of 4 MPa  for the purpose of receiving commercial hydrogen and other process gases.

It is designed for loading into top layer of mining reactor of the second step of steam-air reforming of natural gas under pressure up to 40 atm. The purpose of application is stabilization of burning area and protection of bottom layer of nickel catalyst from abrupt “thermal shock” The catalyst represents chromium oxide applied on corundum, which are macroporous and granulous.

Catalyst of methanation TO-2 is designed for purification of hydronitric mixture from carbonic oxide.

The catalysts «OXK-02» and «OXK-02E» are  designed for steam reforming of  carbonic oxide  process  under pressure up to 5 MPa and under the temperatures (320÷350). The production of pilot batch of catalyst «OXK-02» was conducted in 2001 for commercial reactor loading with the purpose of experimental-industrial tests.

It is designed for catalytic process of carbon monoxide steam conversion in ammonia production. It mainly consists of metallic oxide and produced in a shape of cylindrical granules.

«ChPS-03» method of absorber producing includes the combination of activated zinc oxide with magnesium oxide and surfactant agents, and the shaping of granules absorber with after-baking. The absorber «ChPS-03» is produced on operating equipment of catalyst production from zinc oxide, derived from dead-catalyst (zincous absorbers) «GIAP-10».