کد مقاله | کد نشریه | سال انتشار | مقاله انگلیسی | نسخه تمام متن |
---|---|---|---|---|
53222 | 46955 | 2016 | 12 صفحه PDF | دانلود رایگان |
• Fabrication of a membrane reactor for the nitrite hydrogenation.
• Reactor layout allows low hydrogen concentrations in the reaction zone.
• Manipulation of the H/N ratio on the catalyst surface.
• Higher selectivity towards nitrogen than other reactor layouts.
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.
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Journal: Catalysis Today - Volume 273, 15 September 2016, Pages 50–61