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US3965244A Expired / Lapsed US ⏱️ 0.0 years remaining

Selective removal of sulfur compounds from acid gas mixtures containing significant quantities of carbonyl sulfide

Assignee: Shell USA Inc
•
Filing: 1974-11-27
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Granted: 1976-06-22
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Expires: 1994-11-27
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Abstract

Abstract Acidic gases containing H 2 S, CO 2 and substantial concentratiOns of COS are reduced in sulfur content by contacting said gases in a first stage at elevated temperatures with an aqueous polyalkanolamine solution containing at least 20% by weight of a tetramethylene sulfone wherein a substantial portion of the COS present is hydrolyzed to H 2 S and CO 2 , after which the hydrolyzed acid gases consisting substantially of H 2 S and CO 2 are contacted in a second stage with an alkanolamine absorbent for H 2 S under conditions where H 2 S is selectively removed to low levels.

Inventors

  • 👤 James A. Sykes, Jr.

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-25 10:09
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/14; B01D53/1493; B01D53/1406; B01D53/1418; B01D53/1456

Claims Analysis

Total Claims: 16
Claim 1
Independent Claim 217 words
A continuous process for selective removal of sulfur compounds from a feed gas mixture containing CO 2 , H 2 S and at least 50 parts per million of COS which comprises; a. contacting said feed gas mixture in a first stage at a temperature of from 50°C to 90°C with an aqueous polyalkanolamine solution containing at least 20% by weight of a tetramethylene sulfone, said aqueous polyalkanolamine solution being saturated with CO 2 and H 2 S at the partial pressures of said components in the acid gas feed mixture, thereby absorbing and hydrolyzing a substantial portion of the COS present in said acid gas feed mixture to form and maintain a steady state concentration of acid gas consisting substantially of CO 2 and H 2 S in the gas phase of the first stage; b. withdrawing said gas phase from the first stage and contacting it in a second stage with a regenerable H 2 S-selective, aqueous alkanolamine absorbent solution to afford a substantially H 2 S-free, CO 2 -containing treated gas mixture and an absorbent solution loaded with absorbed H 2 S; c. regenerating the H 2 S-loaded absorbent solution thereby liberating H 2 S; and, d. returning the regenerated absorbent into contact with the gas phase in the second stage of the process.
Claim 2
Dependent Claim 217 words
A continuous process for selective removal of sulfur compounds from a feed gas mixture containing CO 2 , H 2 S and at least 50 parts per million of COS which comprises; a. contacting said feed gas mixture in a first stage at a temperature of from 50°C to 90°C with an aqueous polyalkanolamine solution containing at least 20% by weight of a tetramethylene sulfone, said aqueous polyalkanolamine solution being saturated with CO 2 and H 2 S at the partial pressures of said components in the acid gas feed mixture, thereby absorbing and hydrolyzing a substantial portion of the COS present in said acid gas feed mixture to form and maintain a steady state concentration of acid gas consisting substantially of CO 2 and H 2 S in the gas phase of the first stage; b. withdrawing said gas phase from the first stage and contacting it in a second stage with a regenerable H 2 S-selective, aqueous alkanolamine absorbent solution to afford a substantially H 2 S-free, CO 2 -containing treated gas mixture and an absorbent solution loaded with absorbed H 2 S; c. regenerating the H 2 S-loaded absorbent solution thereby liberating H 2 S; and, d. returning the regenerated absorbent into contact with the gas phase in the second stage of the process.
Claim 3
Dependent Claim 40 words
The process of claim 1 wherein the aqueous polyalkanolamine solution employed in the first stage contains 20 to 65% by weight of a tetramethylene sulfone, 20 to 50% by weight of a polyalkanolamine and 5 to 15% by weight water.
Claim 4
Dependent Claim 19 words
The process of claim 2 wherein the total pressure in the first stage ranges between atmospheric and 2000 psig.
Claim 5
Dependent Claim 22 words
The process of claim 2 wherein the tetramethylene sulfone component of the aqueous polyalkanolamine solution employed in the first stage is sulfolane.
Claim 6
Dependent Claim 30 words
The process of claim 4 wherein the polyalkanolamine component of the aqueous polyalkanolamine solution employed in the first stage is selected from the class consisting of di-n-propanolamine, n-propanolisopropanolamine and diisopropanolamine.
Claim 7
Dependent Claim 10 words
The process of claim 5 wherein the polyalkanolamine is diisopropanolamine.
Claim 8
Dependent Claim 84 words
The process of claim 2 wherein the feed gas mixture is contacted with the aqueous polyalkanolamine solution in the first stage in a manner such that the residence time of the gas liquid contact ranges from 5 to 120 seconds and the mole ratio of polyalkanolamine solution in the first stage to gas feed rate to the first stage ranges between 1 and 3 based on the molar quantities of the two components at equivalent gas feed and withdrawal rates from the first stage.
Claim 9
Dependent Claim 75 words
The process of claim 2, wherein the first stage of the process is carried out by countercurrently contacting the gaseous feed mixture with the aqueous polyalkanolamine solution in a vertically oriented column wherein the gaseous feed is introduced just above the bottom of the column and the solution is continuously recirculated from the bottom of the column through a heat exchanger to maintain the desired solution temperature and back into the top of the column.
Claim 10
Dependent Claim 31 words
The process of claim 8, wherein the gaseous feed mixture is passed through a vertically oriented column containing 10-30 contacting trays at a superficial gas velocity of 1 to 3 ft/sec.
Claim 11
Dependent Claim 37 words
The process of claim 2, wherein the gas phase withdrawn from the first stage is cooled to a temperature below 45°C prior to contacting the regenerable H 2 S-selective, aqueous alkanolamine absorbent solution in the second stage.
Claim 12
Dependent Claim 57 words
The process of claim 10, wherein selective H 2 S absorption is effected in the second stage by countercurrent contact of the gas withdrawn from the first stage with an aqueous alkanolamine solution in a tray column having less than 20 contacting trays at a temperature below 45°C and a gas velocity of at least 3 ft/sec.
Claim 13
Dependent Claim 32 words
The process of claim 2, wherein the alkanolamine component of the aqueous alkanolamine absorbent solution employed in the second stage is selected from the class consisting of methyldiethanolamine, triethanolamine, di-n-propanolamine and diisopropanolamine.
Claim 14
Dependent Claim 21 words
The process of claim 12, wherein the aqueous alkanolamine solution employed in the second stage contains a minor amount of sulfolane.
Claim 15
Dependent Claim 11 words
The proccess of claim 13, wherein the alkanolamine component is diisopropanolamine.
Claim 16
Dependent Claim 126 words
The process of claim 14, wherein the first and second stages of the process are carried out in a single segregated column equipped with contacting trays such that the lower segregated portion of the column comprises the first stage of the process wherein the aqueous polyalkanolamine solutin is recirculated in countercurrent contact with the feed gas mixture to give substantial hydrolysis of the gaseous feed mixture and the hydrolyzed gas phase at the top of this lower segregated portion of the column is continuously withdrawn and introduced into the top portion of the column where it is countercurrently contacted with an H 2 S-selective alkanolamine solution under conditions for selective absorption of H 2 S at the steady stage gas composition of the hydrolyzed gas mixture.

References Cited (Backward Citations)

US2083213A Cited
US3098705A Cited
US3266866A Cited
US3347621A Cited
FR2062138A5 Cited
CA947045A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1979-06-22 1979-12-22 1980-06-22 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1983-06-22 1983-12-22 1984-06-22 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1987-06-22 1987-12-22 1988-06-22 $7700.00 Window Closed / Lapsed

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