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US4036943A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for removing sulfur dioxide from a gas and producing sulfur therefrom

Assignee: IFP Energies nouvelles
•
Filing: 1975-11-18
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Granted: 1977-07-19
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Expires: 1995-11-18
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Abstract

Abstract A SO2-containing gas is contacted with an ammonia solution, the resulting ammonium sulfite solution is vaporized to SO2 and NH3 , SO2 is partially reduced to H2S and the resulting gas containing both SO2 and H2S is first contacted with a catalyst to produce sulfur and then made free of sulfur by solvent washing; recovered NH3 is used to re-constitute the ammonia solution.

Inventors

  • 👤 Marie-Jose Huron
  • 👤 Yves Jacquin
  • 👤 Philippe Renault

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-07 23:16
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/34; B01D53/46; B01D53/48; B01D53/50; B01D53/501

Claims Analysis

Total Claims: 16
Claim 1
Independent Claim 254 words
Process for removing sulfur dioxide from a gas containing the same, wherein said gas is contacted, in a first step (a), with an aqueous ammonia absorbing solution, so as to absorb sulfur dioxide in the form of ammonium sulfites, then, in a second step (b), the solution resulting from (a) is heated, so as to decompose the sulfites to a gas containing sulfur dioxide and ammonia, then, in a third step (c), the gas from step (b) is heated at 150°-600° C. with gas capable of reducing SO 2 to H 2 S, in contact with a catalyst for reducing SO 2 to H 2 S so as to produce a gas essentially containing hydrogen sulfide, sulfur dioxide and ammonia in a molar ratio of H 2 S to SO 2 of 1.7-2.3, and in a fourth step (d), the gas from (c), which has a molar ratio H 2 S/SO 2 of from 1.7:1 to 2.3:1 is contacted at 200°-400° C. with a catalyst for the reaction of H 2 S and SO 2 to sulfur, and a gas containing free sulfur, ammonia and residual sulfur dioxide and hydrogen sulfide is recovered, and, in a fifth step (e), said gas recovered from step (d) is cooled to about 150° C. in contact with an organic solvent in the liquid phase, so as to be made free of residual sulfur without substantial formation of ammonium thiosulfate or sulfate, and the resulting ammonia containing effluent gas is used to reconstitute the absorbing solution of (a).
Claim 2
Dependent Claim 254 words
Process for removing sulfur dioxide from a gas containing the same, wherein said gas is contacted, in a first step (a), with an aqueous ammonia absorbing solution, so as to absorb sulfur dioxide in the form of ammonium sulfites, then, in a second step (b), the solution resulting from (a) is heated, so as to decompose the sulfites to a gas containing sulfur dioxide and ammonia, then, in a third step (c), the gas from step (b) is heated at 150°-600° C. with gas capable of reducing SO 2 to H 2 S, in contact with a catalyst for reducing SO 2 to H 2 S so as to produce a gas essentially containing hydrogen sulfide, sulfur dioxide and ammonia in a molar ratio of H 2 S to SO 2 of 1.7-2.3, and in a fourth step (d), the gas from (c), which has a molar ratio H 2 S/SO 2 of from 1.7:1 to 2.3:1 is contacted at 200°-400° C. with a catalyst for the reaction of H 2 S and SO 2 to sulfur, and a gas containing free sulfur, ammonia and residual sulfur dioxide and hydrogen sulfide is recovered, and, in a fifth step (e), said gas recovered from step (d) is cooled to about 150° C. in contact with an organic solvent in the liquid phase, so as to be made free of residual sulfur without substantial formation of ammonium thiosulfate or sulfate, and the resulting ammonia containing effluent gas is used to reconstitute the absorbing solution of (a).
Claim 3
Dependent Claim 24 words
A process according to claim 1, wherein the free sulfur containing gas supplied to step (e) has an ammonia content of 5-60% by volume.
Claim 4
Dependent Claim 24 words
A process according to claim 1, wherein the free sulfur containing gas supplied to step (e) has an ammonia content of 12-40% by volume.
Claim 5
Dependent Claim 26 words
A process according to claim 1, wherein the gas capable of reducing SO 2 to H 2 S comprises a mixture of carbon monoxide and hydrogen.
Claim 6
Dependent Claim 30 words
A process according to claim 1, wherein said free sulfur containing gas is at a temperature not less than about 200° C. prior to being contacted with said organic solvent.
Claim 7
Dependent Claim 78 words
A process according to claim 1, wherein the sulfur dioxide containing gas also contains SO 3 , whereby ammonium sulfates are produced in step (a) in addition to ammonium sulfites, and, after decomposition of the sulfites in step (b), the remainder of the solution, which contains ammonium sulfates, is treated with a reducing agent, so as to convert said ammonium sulfates to SO 2 and NH 3 which are subsequently subjected to the third step of the process.
Claim 8
Dependent Claim 27 words
A process according to claim 6, wherein the treatment of the ammonium sulfates with a reducing agent is carried out in a bath of molten sodium sulfate.
Claim 9
Dependent Claim 43 words
A process according to claim 1, wherein the catalyst of the third step comprises at least one metal or oxide or sulfide thereof, said metal being selected from the metals of groups VI B and VIII of the periodic classification of the elements.
Claim 10
Dependent Claim 23 words
A process according to claim 1, wherein the catalyst of the third step is a mixture of cobalt and molybdenum oxides on alumina.
Claim 11
Dependent Claim 33 words
A process according to claim 1, wherein the catalyst of the third step comprises at least one metal or oxide or sulfide thereof, the metal being copper, silver, vanadium, manganese, rhenium or zinc.
Claim 12
Dependent Claim 17 words
A process according to claim 1, wherein the temperature of the third step is about 450° C.
Claim 13
Dependent Claim 17 words
A process according to claim 1, wherein the catalyst of the fourth step is alumina or bauxite.
Claim 14
Dependent Claim 17 words
A process according to claim 1, wherein the organic solvent of the fifth step is polyetylene glycol.
Claim 15
Dependent Claim 32 words
A process according to claim 1, wherein the gas capable of reducing SO 2 to H 2 S is a gas comprising either methane or a mixture of carbon monoxide and hydrogen.
Claim 16
Dependent Claim 20 words
A process according to claim 1, wherein the gas capable of reducing SO 2 to H 2 S comprises methane.

References Cited (Backward Citations)

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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) 1980-07-18 1981-01-17 1981-07-19 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1984-07-18 1985-01-17 1985-07-19 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1988-07-18 1989-01-17 1989-07-19 $7700.00 Window Closed / Lapsed

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