US4425317A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Recycle of hydrogenated sulfur plant tail gas to sour gas scrubbing system
Assignee: Linde GmbH
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Filing: 1981-12-08
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Granted: 1984-01-10
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Expires: 2001-12-08
Abstract
Abstract In a process for the separation of at least carbon dioxide and hydrogen sulfide from a raw gaseous mixture to form a purified gaseous mixture comprising passing said gas through a sour gas removal system including the steps of scrubbing said gaseous mixture with a liquid scrubbing agent having a higher affinity for hydrogen sulfide than for carbon dioxide, removing from said system an off-gas enriched in hydrogen sulfide, and passing said off-gas to a sulfur recovery system comprising the conversion of sulfur values to elemental sulfur and the recovery of a tail gas containing hydrogen sulfide and sulfur dioxide, the improvement which comprises hydrogenating said tail gas to convert sulfur dioxide to hydrogen sulfide and recycling resultant hydrogenated tail gas to said sour gas removal system, whereby essentially no hydrogen sulfide or sulfur dioxide is discharged into the environment.
Inventors
- 👤 Rainer Zeller
- 👤 Aldo Belloni
- 👤 Michael Heisel
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-24 19:11
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/14; B01D53/1456; B01D53/1462; C; C01; C01B; C01B17/00; C01B17/02; C01B17/04; C01B17/0404; C01B17/0456; Y; Y02; Y02C; Y02C20/00; Y02C20/40; Y02P; Y02P20/00; Y02P20/151
Claims Analysis
Total Claims: 13
Claim 1
Independent Claim
172 words
In a process for the separation of at least carbon dioxide and hydrogen sulfide from a raw gaseous mixture to form a purified gaseous mixture comprising passing said gas through a sour gas removal system including the steps of scrubbing said gaseous mixture with a physical liquid scrubbing agent having a higher absorbability for hydrogen sulfide than for carbon dioxide, removing from said system an off-gas enriched in hydrogen sulfide, and passing said off-gas to a sulfur recovery system comprising the conversion of sulfur values to elemental sulfur and the recovery of a tail gas containing hydrogen sulfide and sulfur dioxide, the improvement which comprises hydrogenating said tail gas to convert sulfur dioxide to hydrogen sulfide and recycling resultant hydrogenated tail gas to said sour gas removal system, said sour gas removal system comprising in series a scrubbing column, a hydrogen-sulfide enrichment column, and a regeneration column, said resultant hydrogenated tail gas being recycled into the hydrogen-sulfide enrichment column, whereby essentially no hydrogen sulfide or sulfur dioxide is discharged into the environment.
Claim 2
Dependent Claim
172 words
In a process for the separation of at least carbon dioxide and hydrogen sulfide from a raw gaseous mixture to form a purified gaseous mixture comprising passing said gas through a sour gas removal system including the steps of scrubbing said gaseous mixture with a physical liquid scrubbing agent having a higher absorbability for hydrogen sulfide than for carbon dioxide, removing from said system an off-gas enriched in hydrogen sulfide, and passing said off-gas to a sulfur recovery system comprising the conversion of sulfur values to elemental sulfur and the recovery of a tail gas containing hydrogen sulfide and sulfur dioxide, the improvement which comprises hydrogenating said tail gas to convert sulfur dioxide to hydrogen sulfide and recycling resultant hydrogenated tail gas to said sour gas removal system, said sour gas removal system comprising in series a scrubbing column, a hydrogen-sulfide enrichment column, and a regeneration column, said resultant hydrogenated tail gas being recycled into the hydrogen-sulfide enrichment column, whereby essentially no hydrogen sulfide or sulfur dioxide is discharged into the environment.
Claim 3
Dependent Claim
24 words
A process according to claim 1, wherein the physical scrubbing agent having a higher absorbability for hydrogen sulfide than for carbon dioxide is methanol.
Claim 4
Dependent Claim
73 words
A process according to claim 1, said raw gaseous mixture further comprising hydrogen, and further comprising the steps of withdrawing loaded scrubbing agent from the scrubbing column of the sour gas removal system, expanding said loaded scrubbing agent to a lower pressure, separating a liquid phase and a hydrogen-containing gas phase from said expanded loaded scrubbing agent, and employing said gas phase at least in part for said hydrogenating of said tail gas.
Claim 5
Dependent Claim
17 words
A process according to claim 3, further comprising passing said liquid phase to the hydrogen-sulfide enrichment column.
Claim 6
Dependent Claim
24 words
A process according to claim 3, wherein the physical scrubbing agent having a higher absorbability for hydrogen sulfide than for carbon dioxide is methanol.
Claim 7
Dependent Claim
24 words
A process according to claim 4, wherein the physical scrubbing agent having a higher absorbability for hydrogen sulfide than for carbon dioxide is methanol.
Claim 8
Dependent Claim
31 words
A process according to claim 1, further comprising introducing a gaseous nitrogen stream into the bottom of the hydrogen-sulfide enrichment column to strip out CO 2 from the physical scrubbing agent.
Claim 9
Dependent Claim
31 words
A process according to claim 3, further comprising introducing a gaseous nitrogen stream into the bottom of the hydrogen-sulfide enrichment column to strip out CO 2 from the physical scrubbing agent.
Claim 10
Dependent Claim
17 words
A process according to claim 8, further comprising passing said liquid phase to the hydrogen-sulfide enrichment stage.
Claim 11
Dependent Claim
24 words
A process according to claim 9, wherein the physical scrubbing agent having a higher absorbability for hydrogen sulfide than for carbon dioxide is methanol.
Claim 12
Dependent Claim
16 words
A process according to claim 1, wherein the conversion to sulfur is about 85 to 97%.
Claim 13
Dependent Claim
16 words
A process according to claim 10, wherein the conversion to sulfur is about 91 to 95%.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1987-01-09 | 1987-07-11 | 1988-01-10 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1991-01-09 | 1991-07-11 | 1992-01-10 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1995-01-09 | 1995-07-11 | 1996-01-10 | $7700.00 | Window Closed / Lapsed |