Participants
| Role | Name | HCID | Charge |
|---|
| Reactant | Ammonia | HCID 222 | — |
| Reactant | Nitrate | HCID 943 | — |
| Reactant | Sulfur Dioxide | HCID 1119 | — |
| Reactant | Ammonium Sulfate | HCID 6097028 | — |
| Solvent | Water | HCID 962 | — |
| Product | Ammonium nitrate | HCID 22985 | — |
| Product | Ammonium Sulfate | HCID 6097028 | — |
Reaction Steps
One commercial process uses ammonia to simultaneously remove SO2 and NOx within one reactor and produce mixed ammonium sulfate and nitrate fertilizer. This process is described in R. R. Lunt and J. D. Curic, Profiles in Flue Gas Desulfurization, 76-77, American Institute of Chemical Engineers (2000). Flue gas is first partially saturated and cooled with water to a temperature of 150°±10° F. The flue gas is subsequently mixed with ammonia and passed to the reactor where the flue gas-ammonia mixture is subjected to beams of high energy electrons to oxidize the sulfur dioxide and NOx. These oxidized species subsequently react with the ammonia to form ammonium sulfate and ammonium nitrate particulate. This process does not address the greenhouse gas (CO2) capture and removal problem. Further, the process gives an undesirable trace byproduct, ammonium sulfamate, which is harmful to crops. Finally, the process is expensive.
Provenance & Evidence
| DOI | 10.6084/m9.figshare.5104873.v1 |
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| Patent number | US07255842B1 |
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| Source dataset | uspto-grants-2007_08 |
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| ORD ID | ord-d9a455421800478ca60f703746c9a631 |
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| Source note | uspto-grants-2007_08 |
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