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US4714480A Expired / Lapsed US ⏱️ 0.0 years remaining

Removal of acid gases from a gas mixture

Assignee: Shell USA Inc
•
Filing: 1986-12-15
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Granted: 1987-12-22
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Expires: 2006-12-15
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Abstract

Abstract Process for selectively removing H 2 S from a gas mixture including H 2 S and CO 2 comprising contacting the gas mixture in a first contacting zone (1) with lean absorbent to obtain loaded absorbent, heating in heat exchanger (15) loaded absorbent, flashing in separating vessel (5) the heated loaded absorbent to obtain a partly purified absorbent and a CO 2 -rich gas mixture, contacting the CO 2 -rich gas mixture with a lean absorbent in second contacting zone (7) to obtain H 2 S-loaded absorbent, adding the H 2 S-loaded absorbent to the loaded absorbent before heating, and regenerating the partly purified absorbent in a regenerating zone (9) to obtain lean absorbent and H 2 S-rich gas.

Inventors

  • 👤 Derk H. N. Wansink

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-24 17:08
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/14; B01D53/1456; B01D53/1462; Y; Y02; Y02C; Y02C20/00; Y02C20/40

Claims Analysis

Total Claims: 6
Claim 1
Independent Claim 211 words
A process for the selective removal of H 2 S from a gas mixture containing H 2 S and CO 2 , comprising: (a) contacting in a first contact zone at elevated pressure the gas mixture with a lean and regenerable absorbent, from which zone purified gas mixture and a first loaded absorbent containing H 2 S and CO 2 are removed; (b) heating the first loaded absorbent and flashing in a separating vessel at reduced pressure a substantially CO 2 -containing off-gas including a minor amount of H 2 S from the first loaded absorbent, from which separating vessel off-gas and partly loaded absorbent are removed; (c) contacting in a second contact zone the off-gas with a lean and regenerable absorbent that selectively absorbs H 2 S, from which zone an almost H 2 S-free CO 2 -containing gas mixture and a second loaded absorbent are removed; (d) adding the second loaded absorbent to the first loaded absorbent in the separating vessel or upstream of the heating in step (b); (e) introducing the partly loaded absorbent from steps (b) and (d) into a regeneration zone and obtaining a regenerated absorbent used as the lean and regenerable absorbent in steps (a) and (c), and a substantially H 2 S-containing gas mixture.
Claim 2
Dependent Claim 211 words
A process for the selective removal of H 2 S from a gas mixture containing H 2 S and CO 2 , comprising: (a) contacting in a first contact zone at elevated pressure the gas mixture with a lean and regenerable absorbent, from which zone purified gas mixture and a first loaded absorbent containing H 2 S and CO 2 are removed; (b) heating the first loaded absorbent and flashing in a separating vessel at reduced pressure a substantially CO 2 -containing off-gas including a minor amount of H 2 S from the first loaded absorbent, from which separating vessel off-gas and partly loaded absorbent are removed; (c) contacting in a second contact zone the off-gas with a lean and regenerable absorbent that selectively absorbs H 2 S, from which zone an almost H 2 S-free CO 2 -containing gas mixture and a second loaded absorbent are removed; (d) adding the second loaded absorbent to the first loaded absorbent in the separating vessel or upstream of the heating in step (b); (e) introducing the partly loaded absorbent from steps (b) and (d) into a regeneration zone and obtaining a regenerated absorbent used as the lean and regenerable absorbent in steps (a) and (c), and a substantially H 2 S-containing gas mixture.
Claim 3
Dependent Claim 22 words
A process according to claim 1, wherein the second loaded absorbent is added to the first loaded absorbent in the separating vessel.
Claim 4
Dependent Claim 21 words
A process according to claim 1, wherein the second loaded absorbent is added to the first loaded absorbent before being heated.
Claim 5
Dependent Claim 19 words
A process according to claim 1, wherein the absorbent is an aliphatic tertiary amine or aliphatic tertiary alkanol amine.
Claim 6
Dependent Claim 30 words
A process according to claim 1, wherein the initial gas mixture to be purified has a ratio of the volume parts of H 2 S and CO 2 of 1:50.

References Cited (Backward Citations)

US2860030A Cited
US3630666A Cited
US4407784A Cited
GB2103645A Cited
US4397660A Cited
DE3408851A1 Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1990-12-21 1991-06-22 1991-12-22 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1994-12-21 1995-06-22 1995-12-22 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1998-12-21 1999-06-22 1999-12-22 $7700.00 Window Closed / Lapsed

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