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US4201752A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for the selective removal of sulfur dioxide from effluent gases

Assignee: Katalistiks International Inc
•
Filing: 1979-03-01
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Granted: 1980-05-06
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Expires: 1999-03-01
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Abstract

Abstract Method for scrubbing SO2 from effluent gases using aqueous monoethanolamine and the corresponding sulfite as the solvent. The method is especially useful where the effluent gases contain an abundance of CO2 relative to SO2.

Inventors

  • 👤 Alexander J. M. Kosseim
  • 👤 Gilbert R. Atwood
  • 👤 Joseph E. Sokolik, Jr.

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-07 06:11
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/34; B01D53/46; B01D53/48; B01D53/50; B01D53/507; B01D53/14; B01D53/1456; B01D53/1493; Y; Y02; Y02C; Y02C20/00; Y02C20/40

Claims Analysis

Total Claims: 7
Claim 1
Independent Claim 271 words
The process for the selective removal of sulfur oxides from gas mixtures containing at least such sulfur oxides and carbon dioxide which comprises: (a) passing the gas mixture at a temperature below 80° C. through an absorber in countercurrent contact with an absorbent solvent composition consisting essentially of (1) from about 20 to about 60% by weight of monoethanolamine; (2) from about 10 to about 40% by weight of sulfur dioxide such that the molar ratio of sulfur dioxide to available monoethanolamine is always greater than or equal to 0.5/1; and (3) at least about 4% by weight water at a solvent composition flow to gas flow ratio such that the molar concentration of sulfur oxides to be absorbed therein does not exceed the molar concentration of water present; (b) absorbing said sulfur oxides in said solvent composition; (c) passing the aborbent solvent composition containing absorbed sulfur oxides at a maximum temperature of about 120° C., to at least one stripper tower and stripping the absorber sulfur dioxide from the absorbent solvent composition while maintaining the temperature in the stripper below 120° C.; (d) removing from the stripper a stripped lean solvent bottom composition containing a maximum of about 40% by weight of sulfur dioxide and at least about one mole of water for each mole of sulfur oxides remaining in said lead solvent; (e) recycling the stripped lean solvent bottoms from step (d) to the absorber together with sufficient water to provide a solvent absorbent composition having the same composition as defined in step (a); and (f) removing from the stripper a vapor consisting essentially of sulfur dioxide and water.
Claim 2
Dependent Claim 271 words
The process for the selective removal of sulfur oxides from gas mixtures containing at least such sulfur oxides and carbon dioxide which comprises: (a) passing the gas mixture at a temperature below 80° C. through an absorber in countercurrent contact with an absorbent solvent composition consisting essentially of (1) from about 20 to about 60% by weight of monoethanolamine; (2) from about 10 to about 40% by weight of sulfur dioxide such that the molar ratio of sulfur dioxide to available monoethanolamine is always greater than or equal to 0.5/1; and (3) at least about 4% by weight water at a solvent composition flow to gas flow ratio such that the molar concentration of sulfur oxides to be absorbed therein does not exceed the molar concentration of water present; (b) absorbing said sulfur oxides in said solvent composition; (c) passing the aborbent solvent composition containing absorbed sulfur oxides at a maximum temperature of about 120° C., to at least one stripper tower and stripping the absorber sulfur dioxide from the absorbent solvent composition while maintaining the temperature in the stripper below 120° C.; (d) removing from the stripper a stripped lean solvent bottom composition containing a maximum of about 40% by weight of sulfur dioxide and at least about one mole of water for each mole of sulfur oxides remaining in said lead solvent; (e) recycling the stripped lean solvent bottoms from step (d) to the absorber together with sufficient water to provide a solvent absorbent composition having the same composition as defined in step (a); and (f) removing from the stripper a vapor consisting essentially of sulfur dioxide and water.
Claim 3
Dependent Claim 13 words
A process according to claim 1 wherein the sulfur oxide is sulfur dioxide.
Claim 4
Dependent Claim 27 words
A process according to claim 1 for removal of sulfur oxides and nitrogen oxides from gas mixtures containing at least sulfur oxides, nitrogen oxides and carbon dioxide.
Claim 5
Dependent Claim 26 words
A process according to claim 1 wherein the gas mixture is passed through an absorber at a temperature in the range of 30° to 50° C.
Claim 6
Dependent Claim 21 words
A process according to claim 1 wherein the temperature of the stripper is in the range of 80° to 100° C.
Claim 7
Dependent Claim 20 words
A process according to claim 1 wherein the gas mixture contains an abundance of carbon dioxide relative to sulfur oxides.

References Cited (Backward Citations)

US3719742A Cited
US3790660A Cited
US3873673A Cited
US3904735A Cited
US4071602A Cited
US4113849A Cited
US4122149A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1983-05-06 1983-11-05 1984-05-06 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1987-05-06 1987-11-05 1988-05-06 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1991-05-06 1991-11-05 1992-05-06 $7700.00 Window Closed / Lapsed

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