Patent US3943228A successfully refreshed from Google Patents.
US3943228A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for efficiently purifying industrial gas
Assignee: IFP Energies nouvelles
•
Filing: 1973-11-27
•
Granted: 1976-03-09
•
Expires: 1993-11-27
Abstract
Abstract Sulfur dioxide and ammonia remaining in waste-gas after partial purification thereof, for example by means of ammonia or ammonium sulfite solutions, are withdrawn from said gas by washing with a diluted aqueous solution of ammonium sulfate; the resulting ammonium sulfite containing solution is oxidized thereafter either by means of air or in an electrochemical cell.
Inventors
- 👤 Claude Dezael
- 👤 Jean-Pierre Poitevin
- 👤 Philippe Renault
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-06 14:35
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/34; C; C01; C01C; C01C1/00; C01C1/24; C01C1/245; C01C1/246
Claims Analysis
Total Claims: 9
Claim 1
Independent Claim
264 words
A process for efficiently removing sulfur dioxide and ammonia from an industrial waste gas containing each of them in a proportion lower than about 300 ppm by volume, comprising the steps of: a. contacting the waste gas with a dilute aqueous solution of ammonium sulfate, to absorb sulfur dioxide and ammonia and form ammonium sulfites dissolved in said dilute ammonium sulfate solution at a concentration of about 0.02-0.5 mole of ammonium sulfite per liter; b. separating resultant purified gas from the solution obtained in step (a); c. dividing the separated solution into separate portions; d. passing a first portion of separated solution to the anodic compartment of an electrochemical cell having a cation-permeable membrane separating the anodic compartment from the cathodic compartment, and passing a second portion of said separated solution to the cathodic compartment of said cell and electrolyzing said portions in said compartments to convert sulfite to sulfate in the anodic compartment and transfer ammonium ions through said cation-permeable membrane to produce a solution of neutral ammonium sulfite in the cathodic compartment; e. discharging the solution of neutral ammonium sulfite from the cathodic compartment and thereafter contacting it with a molecular oxygen containing gas, thereby converting said neutral ammonium sulfite to ammonium sulfate; f. admixing at least a fraction of the solution discharged from the anodic compartment with at least a fraction of the solution discharged from the cathodic compartment and subsequently contacted with a molecular oxygen containing gas; and g. recycling at least a portion of said admixed fractions to the step (a) as the dilute aqueous solution of ammonium sulfate.
Claim 2
Dependent Claim
264 words
A process for efficiently removing sulfur dioxide and ammonia from an industrial waste gas containing each of them in a proportion lower than about 300 ppm by volume, comprising the steps of: a. contacting the waste gas with a dilute aqueous solution of ammonium sulfate, to absorb sulfur dioxide and ammonia and form ammonium sulfites dissolved in said dilute ammonium sulfate solution at a concentration of about 0.02-0.5 mole of ammonium sulfite per liter; b. separating resultant purified gas from the solution obtained in step (a); c. dividing the separated solution into separate portions; d. passing a first portion of separated solution to the anodic compartment of an electrochemical cell having a cation-permeable membrane separating the anodic compartment from the cathodic compartment, and passing a second portion of said separated solution to the cathodic compartment of said cell and electrolyzing said portions in said compartments to convert sulfite to sulfate in the anodic compartment and transfer ammonium ions through said cation-permeable membrane to produce a solution of neutral ammonium sulfite in the cathodic compartment; e. discharging the solution of neutral ammonium sulfite from the cathodic compartment and thereafter contacting it with a molecular oxygen containing gas, thereby converting said neutral ammonium sulfite to ammonium sulfate; f. admixing at least a fraction of the solution discharged from the anodic compartment with at least a fraction of the solution discharged from the cathodic compartment and subsequently contacted with a molecular oxygen containing gas; and g. recycling at least a portion of said admixed fractions to the step (a) as the dilute aqueous solution of ammonium sulfate.
Claim 3
Dependent Claim
29 words
A process according to claim 1, wherein a portion of the admixed solutions of step (f) is discharged and water is added to the recycled portion of step (g).
Claim 4
Dependent Claim
23 words
A process according to claim 1 wherein the dilute aqueous solution of ammonium sulfate has a concentration of about 1 mole per liter.
Claim 5
Dependent Claim
29 words
A process according to claim 1, wherein the ammonium sulfate concentration of the solution of step (a) is in the range of from 0.05 to 3 moles per liter.
Claim 6
Dependent Claim
32 words
A process according to claim 1, wherein the waste gas is a gas obtained by washing a sulfur dioxide containing gas by means of an aqueous solution of ammonia or ammonium sulfite.
Claim 7
Dependent Claim
16 words
a process according to claim 1, wherein the contact of step (a) is carried out counter-currently.
Claim 8
Dependent Claim
25 words
A process according to claim 1, wherein the waste gas contains 50-250 ppm by volume of sulfur dioxide and 50-250 ppm by volume of ammonia.
Claim 9
Dependent Claim
20 words
A process according to claim 1, wherein the contact of step (a) is carried out at a temperature of 40°-70°C.
References Cited (Backward Citations)
US1992681A
Cited
GB356757A
Cited
US1986889A
Cited
US2862789A
Cited
GB826221A
Cited
GB1104583A
Cited
US3510253A
Cited
US3515513A
Cited
US3645671A
Cited
US3676059A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1979-03-09 | 1979-09-08 | 1980-03-09 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1983-03-09 | 1983-09-08 | 1984-03-09 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1987-03-09 | 1987-09-08 | 1988-03-09 | $7700.00 | Window Closed / Lapsed |