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 main components of the TMC-3/1, TMC-3/1-K and TMC- 3/1-KC catalysts are CuO, ZnO and Al₂O₃. An active component of the catalysts after their reduction is copper. Alumina is a structural promoter of the catalysts. Zinc oxide increases the catalysts` resistance against poisoning by sulfur and chlorine compounds. The TMC-3/1-K catalyst is promoted with potassium. The TMC-3/1-KC catalyst is promoted with potassium and cesium. Potassium increases the selectivity of the catalysts and their resistance to poisoning by chlorine compounds. Cesium additionally enhances the catalysts selectivity and activity. The catalysts are delivered in oxidized form. The active form of the catalysts is formed at the time of reduction CuO to Cu carried out in a commercial shift converter.

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

The TZC-3/1 iron-chromium-copper catalyst is the catalyst of co-precipitated type. The main component of the catalyst in its unreduced form is iron(III) oxide. Chromium(III) oxide is a stabilizer and promoter of the catalyst. Copper(II) oxide enhances the catalyst selectivity and, to some extent, its activity. The catalyst is produced in the form of tablets with flat or convexed ends. TZC-3/1 catalyst is delivered in an oxidized form. An active form of the catalyst comprising Fe₃O₄, Cr₂O₃ and CuO is formed as the result of the reduction carried out in a commercial shift converters.