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US4590048A Expired / Lapsed US ⏱️ 0.0 years remaining

Removal of sulfur oxides from gas streams with ammonium sulfite

Assignee: MILPAT Corp 614 NORTH EASTON ROAD GLENSIDE PA 19038 A CORP OF PA
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Filing: 1984-12-05
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Granted: 1986-05-20
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Expires: 2004-12-05
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Abstract

Abstract A process is disclosed to produce a commercially valuable concentrated nitrogen sulfur solution by scrubbing sulfur dioxide from flue and other gases using ammonium sulfite solution as a scrubbing media. The process also has the capability of removing the sulfur dioxide as an insoluble zinc or calcium salt from the scrubbing solution without having to regenerate, recover and recirculate gaseous ammonia.

Inventors

  • 👤 Albert W. Spitz

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-30 19:58
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/34; B01D53/46; B01D53/48; B01D53/50; B01D53/501

Claims Analysis

Total Claims: 9
Claim 1
Independent Claim 189 words
A process for removal of sulfur oxides from sulfur oxide containing flue gases comprising scrubbing the flue gases in the first stage scrubber with an ammomium sulfite solution to remove most of the sulfur oxides and producing a liquor comprising ammonium sulfite, bisulfite and sulfate salts; recycling the liquor in the first stage scrubber and producing a 40% to 50% solution of dissolved ammonium sulfite, bisulfite and sulfate salts in a first stage reservoir while maintaining the pH between about 5 and 5.8; maintaining the ratio of bisulfite to sulfite between approximately 2.3 to 1 and 1 to 1 without liberating ammonia; removing portions of the 40% to 50% solution of dissolved salts from the first stage reservoir; scrubbing the flue gases in a second stage scrubber with an ammonium sulfite solution of pH between 6.2 and 6.8 to remove additional sulfur oxides and producing a dilute liquor of 1% to 10% solids comprising ammonium sulfite, bisulfite and sulfate salts in a second stage reservoir; and pumping the dilute liquor from the second stage reservoir to the first stage reservoir in amounts sufficient to replace the said removed portions.
Claim 2
Dependent Claim 189 words
A process for removal of sulfur oxides from sulfur oxide containing flue gases comprising scrubbing the flue gases in the first stage scrubber with an ammomium sulfite solution to remove most of the sulfur oxides and producing a liquor comprising ammonium sulfite, bisulfite and sulfate salts; recycling the liquor in the first stage scrubber and producing a 40% to 50% solution of dissolved ammonium sulfite, bisulfite and sulfate salts in a first stage reservoir while maintaining the pH between about 5 and 5.8; maintaining the ratio of bisulfite to sulfite between approximately 2.3 to 1 and 1 to 1 without liberating ammonia; removing portions of the 40% to 50% solution of dissolved salts from the first stage reservoir; scrubbing the flue gases in a second stage scrubber with an ammonium sulfite solution of pH between 6.2 and 6.8 to remove additional sulfur oxides and producing a dilute liquor of 1% to 10% solids comprising ammonium sulfite, bisulfite and sulfate salts in a second stage reservoir; and pumping the dilute liquor from the second stage reservoir to the first stage reservoir in amounts sufficient to replace the said removed portions.
Claim 3
Dependent Claim 28 words
The process of claim 1 wherein the maintaining the pH is accomplished by adding a pH maintaining agent selected from the class comprising ammonia and ammonium sulfite solution.
Claim 4
Dependent Claim 40 words
The process of claim 2 further comprising treating the removal portions of the solution with zinc oxide to remove sufficient sulfur dioxide to regenerate the ammonium sulfite by producing an insoluble metal sulfite at pH between approximately 6.5 and 7.0.
Claim 5
Dependent Claim 23 words
The process of claim 2 further comprising treating the removal portions of the solution with calcium hydroxide and recovering the ammonia for reuse.
Claim 6
Dependent Claim 17 words
The process of claim 3 and raising the pH to a value of about 6.5 to 7.
Claim 7
Dependent Claim 17 words
The process of claim 4 and raising the pH to a value of about 6.5 to 7.
Claim 8
Dependent Claim 20 words
The process of claim 3 wherein the treating with zinc oxide is carried on without the release of free ammonia.
Claim 9
Dependent Claim 20 words
The process of claim 4 wherein the treating with calcium hydroxide is carried on without the release of free ammonia.

References Cited (Backward Citations)

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US2862789A Cited
US3579296A Cited
US3503185A Cited
US3929967A Cited
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USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1989-05-19 1989-11-18 1990-05-20 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1993-05-19 1993-11-18 1994-05-20 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1997-05-19 1997-11-18 1998-05-20 $7700.00 Window Closed / Lapsed

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