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EP0082579A1 Expired / Lapsed EP ⏱️ 0.0 years remaining

Self-regulating process for removal of hydrogen sulfide from gases

Assignee: Stauffer Chemical Co
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Filing: 1982-12-21
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Granted: —
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Expires: 2002-12-21
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Abstract

Abstract A self-regulating process for removal of hydrogen sulfide from gases comprising the absorption of a first part of the hydrogen sulfide from the gas stream in an aqueous solution of sulfur dioxide to form elemental sulfur, separation of the remaining amount of hydrogen sulfide from the aas stream bv a conventional absorption system (9), recovery of the hydrogen sulfide from the conventional absorption system, conversion of the recovered hydrogen sulfide to sulfur dioxide and use of the sulfur dioxide to form the aqueous solution of sulfur dioxide used to absorb the first part of the hydrogen sulfide.

Inventors

  • 👤 Manuel Julio Canalas

Bibliographic Details

Application Number —
Jurisdiction EP
Data Source google_patents
Last Synchronized 2026-11-07 21:07
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/14; B01D53/1456; B01D53/1468; B01D53/1418; C; C01; C01B; C01B17/00; C01B17/02; C01B17/04; C01B17/05; C10; C10K; C10K1/00; C10K1/08; C10K1/10; C10K1/102

Claims Analysis

Total Claims: 7
Claim 1
Independent Claim 264 words
A self-regulating process for removing hydrogen sulfide from a hydrogen sulfide-containing gas stream comprising the steps of: a) scrubbing said gas stream with an aqueous solution of sulfur dioxide whereby essentially all of the sulfur dioxide in said aqueous solution is reacted with a portion of the hydrogen sulfide contained therein to form sulfur and water, and the remaining portion of the hydrogen sulfide remains unreacted; b) then scrubbing said gas stream with an absorbent to remove essentially all of the remaining hydrogen sulfide to form an essentially hydrogen sulfide free gas stream and a hydrogen sulfide rich absorbent; c) desorbing said hydrogen sulfide from said hydrogen sulfide rich absorbent to obtain a lean absorbent which is recycled to the hydrogen sulfide absorbent step (b), and a hydrogen sulfide stream; d) Oxidizing said hydrogen sulfide stream to form sulfur dioxide, and dissolving said sulfur dioxide in an aqueous medium to form an aqueous solution of sulfur dioxide and; e) using said aqueous solution of sulfur dioxide as the scrubbing solution in step (a), essentially all of said aqueous solution of sulfur dioxide being used in step (a) and comprising essentially the sole source of sulfur dioxide used in said step; Whereby the amount of hydrogen sulfide which remains after step (a) to be converted to sulfur dioxide is self-regulated so that the reaction between the sulfur dioxide and that portion of the hydrogen sulfide which is not converted to sulfur dioxide to form sulfur and water has the overall effect of consuming essentially all of the hydrogen sulfide contained in the original gas stream.
Claim 2
Dependent Claim 264 words
A self-regulating process for removing hydrogen sulfide from a hydrogen sulfide-containing gas stream comprising the steps of: a) scrubbing said gas stream with an aqueous solution of sulfur dioxide whereby essentially all of the sulfur dioxide in said aqueous solution is reacted with a portion of the hydrogen sulfide contained therein to form sulfur and water, and the remaining portion of the hydrogen sulfide remains unreacted; b) then scrubbing said gas stream with an absorbent to remove essentially all of the remaining hydrogen sulfide to form an essentially hydrogen sulfide free gas stream and a hydrogen sulfide rich absorbent; c) desorbing said hydrogen sulfide from said hydrogen sulfide rich absorbent to obtain a lean absorbent which is recycled to the hydrogen sulfide absorbent step (b), and a hydrogen sulfide stream; d) Oxidizing said hydrogen sulfide stream to form sulfur dioxide, and dissolving said sulfur dioxide in an aqueous medium to form an aqueous solution of sulfur dioxide and; e) using said aqueous solution of sulfur dioxide as the scrubbing solution in step (a), essentially all of said aqueous solution of sulfur dioxide being used in step (a) and comprising essentially the sole source of sulfur dioxide used in said step; Whereby the amount of hydrogen sulfide which remains after step (a) to be converted to sulfur dioxide is self-regulated so that the reaction between the sulfur dioxide and that portion of the hydrogen sulfide which is not converted to sulfur dioxide to form sulfur and water has the overall effect of consuming essentially all of the hydrogen sulfide contained in the original gas stream.
Claim 3
Dependent Claim 15 words
The process of claim 1 wherein said aqueous solution of sulfur dioxide is sulfurous acid.
Claim 4
Dependent Claim 16 words
The process of claim 2 wherein said aqueous solution of sulfur dioxide also contains a buffer.
Claim 5
Dependent Claim 15 words
The process of claim 1 wherein step (a) is conducted at a pressure above atmosphere.
Claim 6
Dependent Claim 20 words
The process of claim 3 wherein the pH of said aqueous solution of sulfur dioxide is less than about 5.
Claim 7
Dependent Claim 26 words
The process of claim 1 wherein said absorbent is monoethanolamine, diethanolamine, methyldiethanolamine, a mixture of tetrahydrothiophene dioxide, diisopropanolamine and water; dimethylether polyethylene glycol or mixtures thereof.

References Cited (Backward Citations)

US1937196A Cited
US1915364A Cited
NL37666C Cited
US2946652A Cited
US4056606A Cited

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