Chilled ammonia based CO
Processes for recovering ammonia from an ammonium sulfate stream include reacting the ammonia sulfate stream with a lime slurry to form a slurry comprising calcium sulfate and ammonia; providing the slurry comprising calcium sulfate and ammonia to a stripper configured to recover the ammonia from the slurry; utilizing a heat source from a chilled ammonia process to the stripper; and extracting an ammonia vapor stream from the stripper. Also disclosed are systems for performing the processes.
1. A process for recovering ammonia from an ammonium sulfate stream, the process comprising:
reacting the ammonium sulfate stream with a lime slurry to form a slurry comprising calcium sulfate and ammonia;
providing the slurry comprising calcium sulfate and ammonia to a stripper configured to recover the ammonia from the slurry;
providing heat to the stripper by a heat source from a chilled ammonia process, wherein a carbon dioxide-lean ammoniated solution from a regenerator in the chilled ammonia process exchanges heat with the slurry comprising calcium sulfate and ammonia; and
extracting an ammonia vapor stream from the stripper.
2. The process of claim 1 , wherein the ammonium sulfate stream is produced by contacting a flue gas comprising sulfur oxides with an aqueous ammonia solution in a sulfur removal device.
3. A process for recovering ammonia from an ammonium sulfate stream, the process comprising:
reacting the ammonium sulfate stream with a lime slurry to form a slurry comprising calcium sulfate and ammonia;
providing the slurry comprising calcium sulfate and ammonia to a stripper configured to recover the ammonia from the slurry;
providing heat to the stripper by a heat source from a chilled ammonia process, wherein an ammonia stripper overhead gas exchanges heat with the slurry comprising calcium sulfate and ammonia; and
extracting an ammonia vapor stream from the stripper.
4. The process of claim 1 , further comprising extracting a calcium sulfate stream from the stripper and introducing the calcium sulfate stream to a gypsum thickener.
5. The process of claim 1 , further comprising providing the ammonia vapor stream to the chilled ammonia process.
6. The process of claim 5 , wherein providing the ammonia vapor stream to the chilled ammonia process comprises feeding the ammonia vapor stream to a carbon dioxide absorber and/or a direct contact cooler.
7. The process of claim 1 , further comprising heating the ammonium sulfate stream with a steam condensate prior to reacting the ammonium sulfate with the lime slurry.
8. A process for recovering ammonia from an ammonium sulfate stream, the process comprising:
reacting the ammonium sulfate stream with a lime slurry to form a slurry comprising calcium sulfate and ammonia;
providing the slurry comprising calcium sulfate and ammonia to a stripper configured to recover the ammonia from the slurry;
providing heat to the stripper by a heat source from a chilled ammonia process; and
extracting an ammonia vapor stream from the stripper; wherein
the ammonium sulfate stream is produced by contacting a cooling liquid comprising sulfur dioxide with an ammoniated solution.