Operando probing of the surface chemistry during the Haber-Bosch process.

The large-scale conversion of N 2 and H 2 into NH 3 (refs.  1,2 ) over Fe and Ru catalysts 3 for fertilizer production occurs through the Haber-Bosch process, which has been considered the most important scientific invention of the twentieth century 4 . The active component of the catalyst enabling the conversion was variously considered to be the oxide 5 , nitride 2 , metallic phase or surface nitride 6 , and the rate-limiting step has been associated with N 2 dissociation 7-9 , reaction of the adsorbed nitrogen 10 and also NH 3 desorption 11 . This range of views reflects that the Haber-Bosch process operates at high temperatures and pressures, whereas surface-sensitive techniques that might differentiate between different mechanistic proposals require vacuum conditions. Mechanistic studies have accordingly long been limited to theoretical calculations 12 . Here we use X-ray photoelectron spectroscopy-capable of revealing the chemical state of catalytic surfaces and recently adapted to operando investigations 13 of methanol 14 and Fischer-Tropsch synthesis 15 -to determine the surface composition of Fe and Ru catalysts during NH 3 production at pressures up to 1 bar and temperatures as high as 723 K. We find that, although flat and stepped Fe surfaces and Ru single-crystal surfaces all remain metallic, the latter are almost adsorbate free, whereas Fe catalysts retain a small amount of adsorbed N and develop at lower temperatures high amine (NH x ) coverages on the stepped surfaces. These observations indicate that the rate-limiting step on Ru is always N 2 dissociation. On Fe catalysts, by contrast and as predicted by theory 16 , hydrogenation of adsorbed N atoms is less efficient to the extent that the rate-limiting step switches following temperature lowering from N 2 dissociation to the hydrogenation of surface species.