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

Goodwin, Christopher M; Lömker, Patrick; Degerman, David; Davies, Bernadette; Shipilin, Mikhail; Garcia-Martinez, Fernando; Koroidov, Sergey; Katja Mathiesen, Jette et al. · Nature · 2024

basic_science · Level V

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Abstract

The large-scale conversion of N<sub>2</sub> and H<sub>2</sub> into NH<sub>3</sub> (refs. <sup>1,2</sup>) over Fe and Ru catalysts<sup>3</sup> for fertilizer production occurs through the Haber-Bosch process, which has been considered the most important scientific invention of the twentieth century<sup>4</sup>. The active component of the catalyst enabling the conversion was variously considered to be the oxide<sup>5</sup>, nitride<sup>2</sup>, metallic phase or surface nitride<sup>6</sup>, and the rate-limiting step has been associated with N<sub>2</sub> dissociation<sup>7-9</sup>, reaction of the adsorbed nitrogen<sup>10</sup> and also NH<sub>3</sub> desorption<sup>11</sup>. 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<sup>12</sup>. Here we use X-ray photoelectron spectroscopy-capable of revealing the chemical state of catalytic surfaces and recently adapted to operando investigations<sup>13</sup> of methanol<sup>14</sup> and Fischer-Tropsch synthesis<sup>15</sup>-to determine the surface composition of Fe and Ru catalysts during NH<sub>3</sub> 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<sub>x</sub>) coverages on the stepped surfaces. These observations indicate that the rate-limiting step on Ru is always N<sub>2</sub> dissociation. On Fe catalysts, by contrast and as predicted by theory<sup>16</sup>, hydrogenation of adsorbed N atoms is less efficient to the extent that the rate-limiting step switches following temperature lowering from N<sub>2</sub> dissociation to the hydrogenation of surface species.