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US3985860A Expired / Lapsed US ⏱️ 0.0 years remaining

Method for oxidation of SO2 scrubber sludge

Assignee: MW Kellogg Co
•
Filing: 1975-09-22
•
Granted: 1976-10-12
•
Expires: 1995-09-22
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Abstract

Abstract This process provides for the oxidation of calcium sulfite produced from wet scrubbing sulfur oxides to gypsum in an aqueous medium containing magnesium sulfate. The process renders scrubber sludge filterable for further manufacturing use or disposal without use of acidic streams.

Inventors

  • 👤 Bernard G. Mandelik
  • 👤 Walter A. Cronkright

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-02 17:06
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/34; B01D53/46; B01D53/48; B01D53/50; B01D53/501; C; C01; C01F; C01F11/00; C01F11/46; C01F11/464

Claims Analysis

Total Claims: 10
Claim 1
Independent Claim 82 words
In a process for removing sulfur oxides from industrial waste gas by contacting the waste gas with a first aqueous medium containing sodium carbonate, calcium hydroxide, or calcium carbonate and precipitating calcium sulfite as a by-product, the improvement which comprises oxidizing at least part of the precipitated calcium sulfite to calcium sulfate with an oxygen-containing gas at an oxygen partial pressure of from about 2 to about 100 psia in a second aqueous medium containing at least 3 weight percent magnesium sulfate.
Claim 2
Dependent Claim 82 words
In a process for removing sulfur oxides from industrial waste gas by contacting the waste gas with a first aqueous medium containing sodium carbonate, calcium hydroxide, or calcium carbonate and precipitating calcium sulfite as a by-product, the improvement which comprises oxidizing at least part of the precipitated calcium sulfite to calcium sulfate with an oxygen-containing gas at an oxygen partial pressure of from about 2 to about 100 psia in a second aqueous medium containing at least 3 weight percent magnesium sulfate.
Claim 3
Dependent Claim 19 words
The process of claim 1 wherein the first aqueous medium contains calcium hydroxide or calcium carbonate or mixtures thereof.
Claim 4
Dependent Claim 24 words
The process of claim 1 wherein the pH of the second aqueous medium is within a range of from about 5.0 to about 8.0.
Claim 5
Dependent Claim 33 words
The process of claim 1 wherein oxidation of said least part of the precipitated calcium sulfite is carried out under a partial pressure of oxygen from about 2 psia. to about 100 psia.
Claim 6
Dependent Claim 49 words
The process of claim 1 wherein the oxygen-containing gas is air which is passed through the second aqueous medium at a superficial velocity of from about 0.1 feet per second to about 1.0 feet per second and at a pressure of from about 10 psig. to about 100 psig.
Claim 7
Dependent Claim 19 words
The process of claim 2 wherein the second aqueous medium is a minor portion of the first aqueous medium.
Claim 8
Dependent Claim 19 words
The process of claim 2 wherein the second aqueous medium contains a minor portion of the first aqueous medium.
Claim 9
Dependent Claim 28 words
The process of claim 1 wherein oxygen and sulfur dioxide are present in the industrial waste gas at a concentration volume ratio of less than 125 to 1.0.
Claim 10
Dependent Claim 27 words
The process of claim 6 wherein the second aqueous medium contains magnesium sulfate in a concentration of from about 5 weight percent to about 27 weight percent.

References Cited (Backward Citations)

US3808321A Cited
US3883639A Cited
US3914378A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1979-10-12 1980-04-12 1980-10-12 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1983-10-12 1984-04-12 1984-10-12 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1987-10-12 1988-04-12 1988-10-12 $7700.00 Window Closed / Lapsed

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