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US4356161A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for reducing the total sulfur content of a high CO2 -content feed gas

Assignee: Shell USA Inc
•
Filing: 1981-08-24
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Granted: 1982-10-26
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Expires: 2001-08-24
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Abstract

Abstract In the process for reducing the total sulfur content of a high CO 2 -content feed gas stream, the feed gas is first passed to an absorption column. The unabsorbed, high CO 2 -content gas is then routed to a reduction step where it is combined with Claus off-gases and the sulfur compounds are reduced to H 2 S. The treated gas is then passed to a second absorption column and the unabsorbed gas is vented to the atmosphere. The fat solvent from both absorption columns is stripped in a common stripper and the stripped gas is passed to a Claus unit for conversion to elemental sulfur.

Inventors

  • 👤 Harold J. McNamara
  • 👤 Joan A. Schilk

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-31 09:35
CPC Classifications
C; C01; C01B; C01B17/00; C01B17/02; C01B17/04; C01B17/0404; C01B17/0408; B; B01; B01D; B01D53/00; B01D53/34; B01D53/46; B01D53/48; B01D53/50; B01D53/507

Claims Analysis

Total Claims: 8
Claim 1
Independent Claim 296 words
A process for reducing the total sulfur content of a high CO 2 -content feed gas to environmentally acceptable levels comprising: (a) passing a feed gas stream comprising 40 to 95% volume CO 2 , 0.03 to 20% volume H 2 S, and 0.02 to 2% volume COS to a first absorption step where said feed gas stream is contacted with a liquid and regenerable polyalkanolamine absorbent selective for hydrogen sulfide, therein producing an unabsorbed portion and a hydrogen sulfide-enriched polyalkanolamine absorbent; (b) passing said unabsorbed portion of the feed gas stream from step (a) together with a hydrogen- and/or carbon monoxide-containing gas, the off gases from the associated Claus process step (e), and a certain amount of steam over a sulfided Group VI and/or Group VIII metal catalyst supported on an inorganic oxidic carrier in a reduction step wherein the aount of steam is adjusted to reduce the COS concentration in the resulting treated gas to a level below about 0.05% volume; (c) passing the gas stream thus treated in said reduction step (b) to a second absorption step in which said treated gas stream is contacted with a liquid and regenerable polyalkanolamine absorbent under such conditions that the unabsorbed portion of said treated gas stream has below about 0.05% volume total sulfur compounds, discharging the unabsorbed portion of said treated gas stream, optionally after incineration, into the atmosphere, and producing a hydrogen sulfide-enriched polyalkanolamine absorbent; (d) regenerating the hydrogen sulfide-enriched absorbents from absorption steps (a) and (c) by heating and/or stripping and using them again for further absorption of hydrogen sulfide; (e) passing the hydrogen sulfide liberated in the regeneration step (d) to a Claus process step; and (f) passing the off-gases produced in said Claus process step (e) to said reduction step (b).
Claim 2
Dependent Claim 296 words
A process for reducing the total sulfur content of a high CO 2 -content feed gas to environmentally acceptable levels comprising: (a) passing a feed gas stream comprising 40 to 95% volume CO 2 , 0.03 to 20% volume H 2 S, and 0.02 to 2% volume COS to a first absorption step where said feed gas stream is contacted with a liquid and regenerable polyalkanolamine absorbent selective for hydrogen sulfide, therein producing an unabsorbed portion and a hydrogen sulfide-enriched polyalkanolamine absorbent; (b) passing said unabsorbed portion of the feed gas stream from step (a) together with a hydrogen- and/or carbon monoxide-containing gas, the off gases from the associated Claus process step (e), and a certain amount of steam over a sulfided Group VI and/or Group VIII metal catalyst supported on an inorganic oxidic carrier in a reduction step wherein the aount of steam is adjusted to reduce the COS concentration in the resulting treated gas to a level below about 0.05% volume; (c) passing the gas stream thus treated in said reduction step (b) to a second absorption step in which said treated gas stream is contacted with a liquid and regenerable polyalkanolamine absorbent under such conditions that the unabsorbed portion of said treated gas stream has below about 0.05% volume total sulfur compounds, discharging the unabsorbed portion of said treated gas stream, optionally after incineration, into the atmosphere, and producing a hydrogen sulfide-enriched polyalkanolamine absorbent; (d) regenerating the hydrogen sulfide-enriched absorbents from absorption steps (a) and (c) by heating and/or stripping and using them again for further absorption of hydrogen sulfide; (e) passing the hydrogen sulfide liberated in the regeneration step (d) to a Claus process step; and (f) passing the off-gases produced in said Claus process step (e) to said reduction step (b).
Claim 3
Dependent Claim 45 words
The process of claim 1 wherein the unabsorbed portion of the feed gas stream from step (a) contains less than 10% by volume of the H 2 S and greater than 90% by volume of the COS and CO 2 in said feed gas stream.
Claim 4
Dependent Claim 15 words
The process of claim 1 wherein said liquid and regnerable polyalkanolamine absorbent is aqueous methyldiethanolamine.
Claim 5
Dependent Claim 16 words
The process of claim 1 wherein said catalyst is a Co-Mo catalyst on an alumina carrier.
Claim 6
Dependent Claim 16 words
The process of claim 1 wherein said catalyst is a Ni-Mo catalyst on an alumina carrier.
Claim 7
Dependent Claim 100 words
The process of claim 1 wherein the temperature in step (b) is between 200° and 350° C. and the reduced gas mixture obtained in step (b) is cooled to a temperature in the range of from 6° to 60° C. in two steps, the first one being an indirect heat exchange and the second one a direct heat exchange with water, and is thereafter contacted with the liquid, regenerable abosrbent in a layered absorption zone having less than 20 absorption layers at a gas velocity between 0.5 and 3.0 m/sec. with respect to the aerated part of the absorption zone.
Claim 8
Dependent Claim 31 words
The process of claim 1 wherein said free gas stream comprises 40 to 90% volume CO 2 , 0.03 to 10% volume H 2 S and 0.02 to 1% volume COS.

References Cited (Backward Citations)

US3961015A Cited
US3965244A Cited
US3989811A Cited
US4153674A Cited
US4241032A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1985-10-25 1986-04-26 1986-10-26 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1989-10-25 1990-04-26 1990-10-26 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1993-10-25 1994-04-26 1994-10-26 $7700.00 Window Closed / Lapsed

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