Ammonia double-alkali process for removing sulfur oxides from stack gases
AssigneeSmelter Control Research Association, Inc.
InventorsIvor E. Campbell, James M. Henderson, Walter Johnson, William H. Wetherill
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AssigneeSmelter Control Research Association, Inc.
InventorsIvor E. Campbell, James M. Henderson, Walter Johnson, William H. Wetherill
Estimating the term…
An ammonia-based double-alkali process for removing sulfur oxides from stack gases. In this process, usually continuous, stack gases are contacted with an aqueous wash liquid containing ammonium sulfite as a sulfur oxide reactive compound to form a spent absorbent liquor containing bisulfite, sulfite and sulfate salts of ammonia. A portion of the reactive compound is regenerated by reacting the spent scrubbing liquor with a source of calcium ions, usually limestone. During the regeneration, calcium sulfite solids are precipitated as a by-product, any gypsum solids precipitation during the process being tolerated for a time insufficient to degrade substantially process performance. The resultant calcium solids are separated from the regenerated liquor which is returned for further contact with the stack gases, a portion of these solids being recycled to the regeneration stage. The process is preferably regulated by monitoring and controlling of the calcium concentration of the regenerated liquor, upset conditions being corrected by the addition of make-up ammonia during regeneration of the liquor.
A process for removing sulfur oxide from stack gases comprising:
In a process for removing sulfur oxide from stack gases which includes the step of contacting stack gases with an aqueous wash liquid comprising ammonium sulfite as a sulfur oxide reactive compound to form a spent absorbent liquor containing bisulfite, sulfite and sulfate salts of ammonia and regenerating the spent absorbent liquor, the improvement comprising regenerating at least a portion of the reactive compound and precipitating calcium sulfite solids by reacting the spent absorbent liquor with a source of calcium ions, the calcium ion concentration of the regenerated liquor being maintained between about 500 and 800 ppm at substantially all times and the pH of the regenerated liquor being maintained between about 5.5 and 6.2 at substantially all times whereby any gypsum solids precipitation in the process is tolerated for a time insufficient to degrade substantially process performance;
Dependencies are inferred from the claim text.