Abstract
Catalytic hydrogenation of nitrite in drinking water demands control over the selectivity towards nitrogen, minimizing the formation of ammonia. This selectivity is strongly influenced by the H/N ratio of reaction intermediates at the catalyst surface. Therefore, we fabricated a membrane reactor that feeds separately hydrogen gas and a nitrite solution. This allows dosing low but homogeneous hydrogen concentrations along the axial direction of the catalyst bed. As a consequence, low H/N ratios can be achieved, favouring the formation of nitrogen without limiting the nitrite conversion. We demonstrate that this reactor concept offers better nitrogen selectivity than conventional reactor configurations where hydrogen is pre-dissolved in the nitrite solution.
Original language | English |
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Pages (from-to) | 50-61 |
Number of pages | 12 |
Journal | Catalysis today |
Volume | 273 |
DOIs | |
Publication status | Published - 2016 |
Event | 5th International Conference on Structured Catalysts and Reactors, ICOSCAR 2016 - Donostia-San Sebastián, Spain Duration: 22 Jun 2016 → 24 Jun 2016 Conference number: 5 |
Keywords
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