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US4250160A Expired / Lapsed US ⏱️ 0.0 years remaining

Production of ammonium sulfate

Assignee: ExxonMobil Technology and Engineering Co
•
Filing: 1977-08-15
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Granted: 1981-02-10
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Expires: 1997-08-15
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Abstract

Abstract A process for the production of ammonium sulfate in a multistage contactor (or column) inclusive of liquid cyclone recycle. A gas, or gases, which contains sulfur dioxide, e.g., a flue gas, is contacted with ammonia in an oxygen and water environment in a column comprised of three sections (zones). Sulfur dioxide is contacted in vapor phase in a central section of the contactor with a stoichiometric excess of ammonia in the presence of oxygen and water vapor to produce ammonium sulfate. A scrubbing section for the removal of ammonia from the effluent gas by countercurrent contact with water or acid solution is provided in the upper section of the contactor. Liquid cyclones are utilized in the lower section of the contactor where product ammonium sulfate is removed as a slurry, crystalline ammonium sulfate is removed from the slurry, and liquid is returned as recycle to the contactor.

Inventors

  • 👤 James M. Eakman

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-30 14:48
CPC Classifications
C; C01; C01C; C01C1/00; C01C1/24; C01C1/242

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.

References Cited (Backward Citations)

US1508736A Cited
US1986899A Cited
US1934573A Cited
US1992681A Cited
US1931408A Cited
GB377504A Cited
US1986889A Cited
US2095074A Cited
GB1031724A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1984-02-10 1984-08-11 1985-02-10 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1988-02-10 1988-08-11 1989-02-10 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1992-02-10 1992-08-11 1993-02-10 $7700.00 Window Closed / Lapsed

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