Abstract
Effective decomposition of NO to N2 in flue gas can be accomplished by a two-step approach using sorbent/catalyst. No reducing gas is needed. A heteropoly compound, H3PW12O40·6H2O, is used as the sorbent/catalyst in this study. At a space velocity of 5000 h-1,70% of NO in a simulated flue gas is absorbed in the fixed bed at 150 °C. Upon heating the NO-saturated bed to 450 °C (at 150 °C/min), 68.3% of the absorbed NO is decomposed into N2. Based on the results of fixed-bed NO absorption and TGA and IR analyses, the absorption of NO is a bulk reaction where the six H2O linkages in the secondary structure are substituted by three NO linkages, and the Keggin structure (primary structure) is preserved. X-ray diffraction data show that the spatial arrangement in the secondary structure is also preserved with a 5% reduction in the lattice constant. O2 and H2O are needed for NO absorption. SO2 and CO2 have no effects on either absorption or decomposition. The basic rationale for the two-step approach is to concentrate NO from flue gas concentrations (hundreds of ppm) into a bulk solid phase (where the NO partial pressure is of the order of 1 atm) thereby taking advantage of the kinetic law of catalyzed NO decomposition (which is either first or second order with respect to NO partial pressure).
| Original language | English |
|---|---|
| Pages (from-to) | 825-831 |
| Number of pages | 7 |
| Journal | Industrial and Engineering Chemistry Research |
| Volume | 33 |
| Issue number | 4 |
| DOIs | |
| State | Published - Apr 1 1994 |
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