Claims Analysis
Total Claims: 10
Claim 1
Independent Claim
239 words
A process for simultaneously producing ammonium sulfate and removing sulfur dioxide from a sulfur dioxide-containing gas in a distillation column comprised of an upper ammonia scrubbing zone, a central reaction zone, and a lower stripping and crystallization zone that contains at least one vapor-liquid contact tray which comprises: (a) introducing a sulfur dioxide-containing gas and ammonia into said central reaction zone wherein sulfur dioxide, ammonia, water and oxygen react to form an ammonium sulfate-containing solution which flows downward into said lower stripping and crystallization zone; (b) introducing water into the upper ammonia scrubbing zone of said distillation column, said water scrubbing the ascending gases as it flows downward into said central reaction zone; (c) withdrawing a substantially ammonia and sulfur dioxide-free gas overhead from said distillation column; (d) introducing an oxygen-containing gas into the bottom of the lower stripping and crystallization zone of said distillation column; (e) supplying heat to said distillation column; (f) withdrawing a slurry stream of liquid and ammonium sulfate solids from each vapor-liquid contact tray on which such a slurry exists in said lower stripping and crystallization zone; (g) separating a substantial portion of said ammonium sulfate solids from each slurry stream withdrawn from each vapor-liquid contact tray to produce a liquid stream depleted in ammonium sulfate solids; and (h) returning each liquid stream produced from each slurry stream in step (g) to the vapor-liquid contact tray from which the slurry stream was originally withdrawn.
Claim 2
Dependent Claim
239 words
A process for simultaneously producing ammonium sulfate and removing sulfur dioxide from a sulfur dioxide-containing gas in a distillation column comprised of an upper ammonia scrubbing zone, a central reaction zone, and a lower stripping and crystallization zone that contains at least one vapor-liquid contact tray which comprises: (a) introducing a sulfur dioxide-containing gas and ammonia into said central reaction zone wherein sulfur dioxide, ammonia, water and oxygen react to form an ammonium sulfate-containing solution which flows downward into said lower stripping and crystallization zone; (b) introducing water into the upper ammonia scrubbing zone of said distillation column, said water scrubbing the ascending gases as it flows downward into said central reaction zone; (c) withdrawing a substantially ammonia and sulfur dioxide-free gas overhead from said distillation column; (d) introducing an oxygen-containing gas into the bottom of the lower stripping and crystallization zone of said distillation column; (e) supplying heat to said distillation column; (f) withdrawing a slurry stream of liquid and ammonium sulfate solids from each vapor-liquid contact tray on which such a slurry exists in said lower stripping and crystallization zone; (g) separating a substantial portion of said ammonium sulfate solids from each slurry stream withdrawn from each vapor-liquid contact tray to produce a liquid stream depleted in ammonium sulfate solids; and (h) returning each liquid stream produced from each slurry stream in step (g) to the vapor-liquid contact tray from which the slurry stream was originally withdrawn.
Claim 3
Dependent Claim
20 words
A process as defined by claim 1 wherein the water introduced into said upper ammonia scrubbing zone contains sulfuric acid.
Claim 4
Dependent Claim
35 words
A process as defined by claim 1 wherein a sufficient amount of ammonia is introduced into said central reaction zone to provide a molar ratio of ammonia to sulfur dioxide of at least about 2.3:1.
Claim 5
Dependent Claim
23 words
A process as defined by claim 1 wherein said ammonia introduced into said central reaction zone is contained in a waste gas stream.
Claim 6
Dependent Claim
22 words
A process as defined by claim 1 wherein said sulfur dioxide-containing gas introduced into said central reaction zone comprises a flue gas.
Claim 7
Dependent Claim
23 words
A process as defined by claim 1 wherein said oxygen-containing gas introduced into the bottom of said stripping and crystallization zone comprises air.
Claim 8
Dependent Claim
26 words
A process as defined by claim 1 wherein a hydroclone is utilized to separate said ammonium sulfate solids from each slurry stream withdrawn in step (f).
Claim 9
Dependent Claim
20 words
A process as defined by claim 1 wherein said heat is supplied to said distillation column in said oxygen-containing gas.
Claim 10
Dependent Claim
29 words
A process as defined by claim 1 wherein said heat is supplied to said distillation column by introducing superheated steam into the bottom of said stripping and crystallization zone.