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US4552572A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for desulfurization of fuel gas

Assignee: Bechtel Group Inc
•
Filing: 1983-07-26
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Granted: 1985-11-12
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Expires: 2003-07-26
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Abstract

Abstract Apparatus and a method for removal of acid gases from a first gas rich in carbon dioxide and for desulfurizing a second gas lean in carbon dioxide but containing sulfur compounds as impurities. The method includes contacting the first gas with a solvent capable of extracting carbon dioxide and sulfur compounds from the first gas. Then, the solvent containing carbon dioxide is separated from the solvent containing sulfur compounds. The second gas is then contacted with said solvent containing carbon dioxide under conditions sufficient to cause said solvent containing carbon dioxide to extract sulfur compounds from said second gas and to release carbon dioxide. The desulfurized second gas is thereafter separated from the solvent containing sulfur compounds from the second gas.

Inventors

  • 👤 Lionel S. Galstaun

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-07 13:38
CPC Classifications
C; C10; C10K; C10K1/00; C10K1/08; C10K1/16; B; B01; B01D; B01D53/00; B01D53/14; B01D53/1406; B01D53/1456; B01D53/1462; C10K1/165; Y; Y02; Y02C; Y02C20/00; Y02C20/40; Y02P; Y02P20/00; Y02P20/151

Claims Analysis

Total Claims: 16
Claim 1
Independent Claim 200 words
In a system for removal of acid gases from a first gas available at super atmospheric pressure, rich in carbon dioxide and containing hydrogen sulfide, and a second gas rich in carbon monoxide, containing carbon dioxide at a partial pressure lower than in said first gas, and containing hydrogen sulfide, the process comprising the steps of: contacting the first gas with a physical absorption solvent having a high selectivity for hydrogen sulfide in counter-current flow of solvent and the first gas wherein said solvent absorbs carbon dioxide and hydrogen sulfide in a first stage and said solvent absorbs carbon dioxide but not hydrogen sulfide in a second stage and using part of the solvent from the second stage in the first stage, separating the solvent containing carbon dioxide and hydrogen sulfide from the first stage and recovering a hydrogen rich gas from the second stage; separately contacting said second gas with another part of the solvent from the second stage under conditions sufficient to cause said solvent containing carbon dioxide to extract hydrogen sulfide from said second gas and to release carbon dioxide; and separating the desulfurized second gas from the solvent containing hydrogen sulfide for use as a fuel.
Claim 2
Dependent Claim 200 words
In a system for removal of acid gases from a first gas available at super atmospheric pressure, rich in carbon dioxide and containing hydrogen sulfide, and a second gas rich in carbon monoxide, containing carbon dioxide at a partial pressure lower than in said first gas, and containing hydrogen sulfide, the process comprising the steps of: contacting the first gas with a physical absorption solvent having a high selectivity for hydrogen sulfide in counter-current flow of solvent and the first gas wherein said solvent absorbs carbon dioxide and hydrogen sulfide in a first stage and said solvent absorbs carbon dioxide but not hydrogen sulfide in a second stage and using part of the solvent from the second stage in the first stage, separating the solvent containing carbon dioxide and hydrogen sulfide from the first stage and recovering a hydrogen rich gas from the second stage; separately contacting said second gas with another part of the solvent from the second stage under conditions sufficient to cause said solvent containing carbon dioxide to extract hydrogen sulfide from said second gas and to release carbon dioxide; and separating the desulfurized second gas from the solvent containing hydrogen sulfide for use as a fuel.
Claim 3
Dependent Claim 12 words
In a system according to claim 1, wherein the solvent is methanol.
Claim 4
Dependent Claim 24 words
In a system according to claim 1, wherein the solvent is the dimethyl ether of a polyethylene glycol having 3 to 8 ethylene units.
Claim 5
Dependent Claim 13 words
In a system according to claim 1, wherein the solvent is N-methyl pyrolidone.
Claim 6
Dependent Claim 31 words
In a system according to claim 1, wherein the pressure of the first gas is above 250 psig, the solvent being in the temperature range of -20° F. to 100° F.
Claim 7
Dependent Claim 24 words
In a system according to claim 1, wherein is included the step of regenerating the solvent containing sulfur compounds to recover hydrogen sulfide therefrom.
Claim 8
Dependent Claim 55 words
In a system according to claim 1, wherein the step of contacting the first gas with said solvent includes directing the solvent into a first, closed region, the step of contacting the second gas including directing the solvent containing carbon dioxide from said first region into a second, closed region spaced from the first region.
Claim 9
Dependent Claim 25 words
In a system according to claim 7, wherein the first gas and the solvent move in countercurrent relationship to each other in said first region.
Claim 10
Dependent Claim 28 words
In a system according to claim 7, wherein the second gas and the solvent containing carbon dioxide move in countercurrent relationship to each other in said second region.
Claim 11
Dependent Claim 48 words
In a system according to claim 7, wherein the contacting of the first gas includes extracting at least a major part of the hydrogen sulfide from the first gas at a zone in the first region below the zone from which the solvent containing carbon dioxide is removed.
Claim 12
Dependent Claim 65 words
In a system according to claim 7, wherein said step of directing the solvent containing carbon dioxide from said first region includes removing a first part of said solvent containing carbon dioxide for flow to the second region, and returning a second part of the solvent containing carbon dioxide to the first region to provide solvent for removal of hydrogen sulfide from the first gas.
Claim 13
Dependent Claim 40 words
In a system according to claim 7, wherein is included the step of removing from the first region the portion of the first gas substantially free of sulfur for flow to a third region in the preparation of synthesis gas.
Claim 14
Dependent Claim 12 words
In a system according to claim 7, wherein the solvent is methanol.
Claim 15
Dependent Claim 24 words
In a system according to claim 7, wherein the solvent is the dimethyl ether of a polyethylene glycol having 3 to 8 ethylene units.
Claim 16
Dependent Claim 13 words
In a system according to claim 7, wherein the solvent is N-methyl pyrolidone.

References Cited (Backward Citations)

US3245752A Cited
US3664091A Cited
US3824766A Cited
US4050909A Cited
US4080424A Cited
DE2759123A1 Cited
US4332598A Cited
GB2088240A Cited
US4430316A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1988-11-11 1989-05-13 1989-11-12 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1992-11-11 1993-05-13 1993-11-12 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1996-11-11 1997-05-13 1997-11-12 $7700.00 Window Closed / Lapsed

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