US3882222A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for purifying a gas containing oxygenated sulfur compounds and recovering sulfur using ammonia liquors
Assignee: IFP Energies nouvelles
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Filing: 1972-02-24
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Granted: 1975-05-06
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Expires: 1992-02-24
Abstract
Abstract Sulfur dioxide is removed from a gas by contacting the latter with ammonia and water, concentrating and then vaporizing the resulting ammonium sulfite solution, passing the vapors through a heated liquid phase, recovering sulfur and ammonia and recycling ammonia.
Inventors
- 👤 Andre Deschamps
- 👤 Claude Dezael
- 👤 Sigismond Franckowiack
- 👤 Philippe Renault
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-28 11:50
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/34; B01D53/46; B01D53/48; B01D53/50; B01D53/501; C; C01; C01B; C01B17/00; C01B17/02; C01B17/04; C01B17/05
Claims Analysis
Total Claims: 14
Claim 1
Independent Claim
214 words
A PROCESS FOR REMOVING SULFUR DIOXIDE FROM A GAS CONTAINING IT, WHEREIN THE GAS IS CONTACTED WITH AMMONIA AND WATER AT A TEMPERATURE OF FROM 30* TO 80*C SO AS TO OBTAIN A SOLUTION OF AMMONIUM SULFITES IN WHICH THE MOLAR RATIO OF H2O TO AMMONIUM SULFITES (EXPRESSED AS SO2) IS FROM 11 : 1 TO 100 : 1, THE SOLUTION IS CONCENTRATED IN A CONCENTRATION ZONE BY EVAPORATING WATER AT A TEMPERATURE LOWER THAN 100*C SO AS TO OBTAIN A MOLAR RATIO OF H2O TO SO2 OF 4 : 1 TO 10 : 1, THE RESULTING CONCENTRATED SOLUTION IS HEATED UP TO 105*-200:C SO AS TO CONVERT AT LEAST THE MAJOR PORTION OF THE AMMONIUM SULFITES THEREIN INTO A GAS MIXTURE OF SULFUR DIOXIDE, AMMONIA AND STEAM, AND SO AS TO PRODUCE A MORE CONCENTRATED RESIDUAL SOLUTION CONTAINING AMMONIUM SULFATES, SAID RESIDUAL SOLUTION BEING DISCHARGED FROM THE PROCESS, SAID GAS MIXTURE IS THEN PASSED WITH HYDROGEN SULFIDE THROUGH A LIQUID PHASE CONSISTING ESSENTIALLY OF AN ORGANIC SOLVENT, AT A TEMPERATURE OF FROM 120* TO 170*C, SO AS TO PRODUCE SULFUR, SAID SULFUR AND A GAS PHASE CONSISTING ESSENTIALLY OF STEAM AND AMMONIA ARE SEPARATED FROM THE LIQUID PHASE, AND AMMONIA IS RECIRCULATED THROUGH THE ZONE OF CONTACT WITH THE SULFUR DIOXIDE CONTAINING GAS.
Claim 2
Dependent Claim
214 words
A PROCESS FOR REMOVING SULFUR DIOXIDE FROM A GAS CONTAINING IT, WHEREIN THE GAS IS CONTACTED WITH AMMONIA AND WATER AT A TEMPERATURE OF FROM 30* TO 80*C SO AS TO OBTAIN A SOLUTION OF AMMONIUM SULFITES IN WHICH THE MOLAR RATIO OF H2O TO AMMONIUM SULFITES (EXPRESSED AS SO2) IS FROM 11 : 1 TO 100 : 1, THE SOLUTION IS CONCENTRATED IN A CONCENTRATION ZONE BY EVAPORATING WATER AT A TEMPERATURE LOWER THAN 100*C SO AS TO OBTAIN A MOLAR RATIO OF H2O TO SO2 OF 4 : 1 TO 10 : 1, THE RESULTING CONCENTRATED SOLUTION IS HEATED UP TO 105*-200:C SO AS TO CONVERT AT LEAST THE MAJOR PORTION OF THE AMMONIUM SULFITES THEREIN INTO A GAS MIXTURE OF SULFUR DIOXIDE, AMMONIA AND STEAM, AND SO AS TO PRODUCE A MORE CONCENTRATED RESIDUAL SOLUTION CONTAINING AMMONIUM SULFATES, SAID RESIDUAL SOLUTION BEING DISCHARGED FROM THE PROCESS, SAID GAS MIXTURE IS THEN PASSED WITH HYDROGEN SULFIDE THROUGH A LIQUID PHASE CONSISTING ESSENTIALLY OF AN ORGANIC SOLVENT, AT A TEMPERATURE OF FROM 120* TO 170*C, SO AS TO PRODUCE SULFUR, SAID SULFUR AND A GAS PHASE CONSISTING ESSENTIALLY OF STEAM AND AMMONIA ARE SEPARATED FROM THE LIQUID PHASE, AND AMMONIA IS RECIRCULATED THROUGH THE ZONE OF CONTACT WITH THE SULFUR DIOXIDE CONTAINING GAS.
Claim 3
Dependent Claim
14 words
A process according to claim 1, wherein the treated gas also contains sulfuric anhydride.
Claim 4
Dependent Claim
14 words
A process according to claim 1, wherein the solvent is of the glycol type.
Claim 5
Dependent Claim
14 words
A process according to claim 1, wherein the concentrated solution is heated to 120*-160*C.
Claim 6
Dependent Claim
24 words
A process according to claim 4, wherein the molar ratio of the hydrogen sulfide to the gaseous sulfur dioxide is from 1.9 to 2.2.
Claim 7
Dependent Claim
33 words
A process according to claim 1, wherein the molar ratio of H2O to the ammonium sulfites expressed as SO2, is from 11 : 1 to 40 : 1, in the gas contact zone.
Claim 8
Dependent Claim
19 words
A process according to claim 6, wherein the gas contains 0.02 - 10 percent by volume of sulfur dioxide.
Claim 9
Dependent Claim
20 words
A process according to claim 7, wherein the gas also contains 0.001 - 1 percent by volume of sulfuric anhydride.
Claim 10
Dependent Claim
34 words
A process according to claim 1, wherein the sulfur dioxide containing gas is contacted with the ammonium sulfite solution in the concentration zone before being contacted with ammonia and water in the contact zone.
Claim 11
Dependent Claim
25 words
A process according to claim 9, wherein the contact with ammonia is conducted at 35*-50*C and the concentration of the solution is performed at 60*-80*C.
Claim 12
Dependent Claim
104 words
In a process for removing sulfur dioxide from a gas containing it wherein the sulfur dioxide is absorbed in an ammoniacal aqueous solution and has a molar ratio of H2O to ammonium sulfites (expressed as SO2) from 11 : 1 to 100 : 1 and in a subsequent step the resultant solution of ammonium sulfites is converted into a gaseous mixture of sulfur dioxide, ammonia and steam, the improvement which comprises concentrating said ammoniacal solution by evaporating water therefrom at a temperature lower than 100*C so as to obtain a molar ratio of H2O to SO2 of 4 : 1 to 10 : 1.
Claim 13
Dependent Claim
104 words
In a process for removing sulfur dioxide from a gas containing it wherein the sulfur dioxide is absorbed in an ammoniacal aqueous solution and has a molar ratio of H2O to ammonium sulfites (expressed as SO2) from 11 : 1 to 100 : 1 and in a subsequent step the resultant solution of ammonium sulfites is converted into a gaseous mixture of sulfur dioxide, ammonia and steam, the improvement which comprises concentrating said ammoniacal solution by evaporating water therefrom at a temperature lower than 100*C so as to obtain a molar ratio of H2O to SO2 of 4 : 1 to 10 : 1.
Claim 14
Dependent Claim
61 words
A process as defined by claim 11 wherein said conversion of ammonium sulfites is conducted by heating tHe concentrated ammoniacal solution to 105*-200*C to convert at least a major portion of the ammonium sulfites into a gaseous mixture of sulfur dioxide, ammonia and steam, and form a more concentrated residual solution containing ammonium sulfate which is separated from said gaseous mixture.
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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) | 1978-05-05 | 1978-11-04 | 1979-05-06 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1982-05-05 | 1982-11-04 | 1983-05-06 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1986-05-05 | 1986-11-04 | 1987-05-06 | $7700.00 | Window Closed / Lapsed |