“…An unsupported iron–chromium oxide catalyst was used to remove CO from the H 2 stream for the Haber–Bosch ammonia synthesis process because CO is a poison for the ammonia synthesis Fe-based catalyst . The iron–chromium oxide WGS catalyst technology was subsequently applied to control the H 2 /CO ratio of syngas for production of hydrogen from methane steam reforming, methanol synthesis, and Fischer–Tropsch synthesis of hydrocarbons. ,, Until the 1980s, the patent and scientific literature focused on improving the synthesis of the existing iron–chromium oxide catalyst. − Research in the 1980s began to explore, by trial-and-error, the effect of a wide range of promoters to try to stabilize surface area, increase activity, and enhance thermal stability of catalysts under the WGS reaction conditions. The additives can be broadly divided into two categories: chemical promoters (Cu, Rh) − and textural promoters (Cr, Al, Th, Zr, Zn, Mg). − …”