Catalytic oxidation of NO to NO for industrial nitric acid production using Ag-promoted MnO/ZrO catalysts

The Ostwald process is the most common industrial process to produce nitric acid (HNO 3 ). It involves three main steps; ammonia oxidation in air over Pt-Rh gauze catalysts to produce nitric oxide, homogeneous gas-phase conversion of NO to NO 2 , and subsequent absorption of the NO 2 by water to produce nitric acid. Turning the homogeneous gas-phase NO oxidation reaction catalytic may lead to a significant reduction in footprint and capital expenditure. However, no industrial catalyst yet exists for this process. In this work, we focus on catalytic oxidation of NO to NO 2 using silver-promoted manganese on zirconia catalysts at industrially relevant conditions (10% NO, 6% O 2 and 15% H 2 O). Silver was found to promote the low-temperature activity of manganese catalysts in both dry and wet conditions compared to unpromoted manganese. The results demonstrate that manganese catalysts are able to work at low temperatures and concentrations relevant to industrial catalytic oxidation of NO. Low-temperature nitric oxide oxidation using silver promoted manganese catalyst can reduce energy footprint of industrial nitric acid production.