Method for purifying flue gases from combustion plants and then producing urea
A method and apparatus is provided for cleaning flue gases from combustion plants. The method includes removing dust and removing nitrogen from flue gases, bringing flue gases into contact with an aqueous ammonia solution in the presence of an oxidizing agent whereby a reaction solution forms which contains at least ammonium carbonate, heating the reaction solution such that ammonium carbonate decomposes and carbon dioxide and ammonia transfer into the gas atmosphere, and reacting the gaseous carbon dioxide and the gaseous ammonia to form urea. The apparatus includes a device for removing nitrogen and removing dust from the flue gases, a washing device downstream of the device for removing nitrogen and removing dust, a stripper downstream of the washing device, and a urea installation downstream of the stripper.
1. A method of cleaning flue gases from combustion plants, including the steps of:
removing dust and removing nitrogen from the flue gases,
bringing the flue gases into contact with an aqueous ammonia solution in the presence of an oxidizing agent, whereby a reaction solution forms, which contains at least ammonium carbonate,
heating the reaction solution such that ammonium carbonate decomposes and carbon dioxide and ammonia transfer into the gas atmosphere,
reacting the gaseous carbon dioxide and the gaseous ammonia to form urea.
2. The method as claimed in claim 1 , wherein removing dust and removing nitrogen from the flue gases further comprises the removal of sulfur.
3. The method as claimed in claim 1 , wherein the ammonia necessary for the aqueous ammonia solution is produced on site by ammonia synthesis.
4. The method as claimed in claim 1 , wherein ammonium sulfate is separated from the reaction solution after heating the reaction solution, during which ammonium carbonate decomposes.
5. The method as claimed in claim 4 , wherein the separation of the ammonium sulfate is performed by spray drying.
6. The method as claimed in claim 1 , wherein air is used as the oxidizing agent.
7. The method as claimed in claim 1 , wherein excess ammonia from reacting the gaseous carbon dioxide and the gaseous ammonia to form urea is re-circulated for the urea synthesis or for producing the aqueous ammonia solution.