System and method for recomposing ammonia from fly ash
View Patent ↗A system and method for decomposing ammonia from fly ash contaminated with ammonia is provided which includes maintaining the temperature of a bed of ammonia-contaminated fly ash at a decomposition temperature greater than 500° F. and less than 842° F. to decompose the ammonia from the fly ash. In a preferred embodiment, the ammonia-laden fly ash is maintained at a temperatures less than a lowest carbon combustion temperature at which substantial combustion of carbon in fly ash begins to occur. A preferred embodiment includes a first chamber operating at a decomposition temperature greater than 500° F. and less than 842° F. followed by a second chamber operating at a higher carbon combustion temperature for carbon burn-out.
1. An apparatus for removing ammonia from ammonia-laden fly ash containing carbon, the system comprising:
a first chamber to receive ammonia-laden fly ash, the first chamber adapted to maintain the ammonia-laden fly ash at a decomposition temperature both a) greater than 500° F. and less than 800° F. to decompose the ammonia in the ammonia-laden fly ash, and b) less than a lowest carbon combustion temperature of at least 800° F. at which substantial combustion of carbon in the ammonia-laden fly ash begins to occur; and
a second chamber positioned downstream of the first chamber to receive resultant ammonia-free fly ash from the first chamber, the second chamber adapted to maintain the resultant ammonia-free fly ash at a carbon combustion temperature to remove carbon from the fly ash.
2. The apparatus of claim 1 wherein the second chamber is adapted to increase the temperature of the resultant ammonia-free fly ash to the carbon combustion temperature, the carbon combustion temperature being between 1100° F. and 1500° F.
3. The apparatus of claim 1 wherein the temperature of the first chamber is controlled by a temperature control unit.
4. The apparatus of claim 3 wherein the temperature control unit comprises a controller, a thermocouple, and a heat source.
5. The apparatus of claim 4 wherein the heat source is selected from a group consisting of: hot fly ash, hot exhaust gas, a heated air input, a liquefied petroleum gas burner and a natural gas burner.
6. A apparatus for removing ammonia from ammonia-laden fly ash, the system comprising:
a chamber to receive the ammonia-laden fly ash, the chamber adapted to maintain the ammonia-laden fly ash at a decomposition temperature greater than 500° F. and less than 800° F. to decompose the ammonia in the ammonia-laden fly ash.
7. The apparatus of claim 6 wherein the chamber is adapted to maintain the ammonia-laden fly ash at a temperature less than a lowest carbon combustion temperature at which substantial combustion of carbon in fly ash begins to occur.
8. The apparatus of claim 6 wherein the temperature of the chamber is controlled by a temperature control unit.
9. The apparatus of claim 8 wherein the temperature control unit comprises a controller, a thermocouple, and a heat source.
10. The apparatus of claim 9 wherein the heat source is one of hot fly ash, hot exhaust gas, a heated air input, a liquefied petroleum gas burner and a natural gas burner.