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US4041129A Expired / Lapsed US ⏱️ 0.0 years remaining

Removal of acidic gases from hydrocarbon streams

Assignee: Stone and Webster Engineering Corp
•
Filing: 1974-07-23
•
Granted: 1977-08-09
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Expires: 1994-07-23
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Abstract

Abstract An apparatus and process for substantially reducing carbon dioxide and/or hydrogen sulfide levels in a hydrocarbon gas with simultaneous regeneration of reagent materials are disclosed. The process consists of passing the gas through an aqueous sodium hydroxide solution, reacting the effluent liquid with an acidic reagent, stripping the acidic gases therefrom and subjecting the resulting aqueous sodium sulfate solution to an electrolytic process. The apparatus used to carry out the process comprises an acidic gas absorbing unit, means for reacting the resulting effluent liquid, means for stripping the acidic gases and an electrolytic cell to convert soluble alkali metal salts into the corresponding alkali metal hydroxide and acidic reagents.

Inventors

  • 👤 Raymond C. Foster
  • 👤 James J. Humphries, Jr.

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-06 04:36
CPC Classifications
C; C10; C10K; C10K1/00; C10K1/08; C10K1/10; C10K1/12; C10K1/122; B; B01; B01D; B01D53/00; B01D53/14; B01D53/1418; B01D53/1456; B01D53/1462; B01D53/1493; B01D53/32; B01D53/326; B01D53/34; B01D53/46; B01D53/48; B01D53/52; B01D53/526; C07; C07C; C07C7/00; C07C7/148; C07C7/14833; C07C7/1485; B01D2251/00; B01D2251/30; B01D2251/304; B01D2251/60; B01D2251/604; Y; Y02; Y02C; Y02C20/00; Y02C20/40; Y02P; Y02P20/00; Y02P20/151

Claims Analysis

Total Claims: 18
Claim 1
Independent Claim 243 words
In a cyclic process for substantially reducing the carbon dioxide and/or hydrogen sulfide content present as acidic gases in a gas obtained from the cracking of a hydrocarbon selected from the group consisting of gas oil, naphtha and ethane, and said gas further containing undesirable organic impurities therein, with simultaneous regeneration of reagent materials which comprises: a. passing the cracked gas containing the acidic gases through an aqueous sodium hydroxide solution and obtaining an effluent containing the undesirable organic impurities and said acidic gases in converted form; b. reacting said effluent liquid with aqueous sulfuric acid or an aqueous mixture containing sulfuric acid and sodium sulfate in an amount sufficient to substantially liberate the converted acidic gases consisting essentially of hydrogen sulfide and/or carbon dioxide that may be present therein; c. subjecting said treated effluent liquid to a stripping operation to remove any liberated gases therefrom and thereby leaving an aqueous sodium sulfate containing solution; and d. subjecting said resulting aqueous sodium sulfate containing solution to an electrolytic process treatment whereby aqueous sulfuric acid or an aqueous mixture of sulfuric acid and sodium sulfate is collected at the anode and is recycled for utilization in the aforesaid reaction step and aqueous sodium hydroxide which forms at the cathode is collected and recycled for use in the sodium hydroxide treatment step, the improvement which comprises treating the effluent from the alkali metal hydroxide treatment of step (a) to remove substantially all organic impurities therefrom.
Claim 2
Dependent Claim 243 words
In a cyclic process for substantially reducing the carbon dioxide and/or hydrogen sulfide content present as acidic gases in a gas obtained from the cracking of a hydrocarbon selected from the group consisting of gas oil, naphtha and ethane, and said gas further containing undesirable organic impurities therein, with simultaneous regeneration of reagent materials which comprises: a. passing the cracked gas containing the acidic gases through an aqueous sodium hydroxide solution and obtaining an effluent containing the undesirable organic impurities and said acidic gases in converted form; b. reacting said effluent liquid with aqueous sulfuric acid or an aqueous mixture containing sulfuric acid and sodium sulfate in an amount sufficient to substantially liberate the converted acidic gases consisting essentially of hydrogen sulfide and/or carbon dioxide that may be present therein; c. subjecting said treated effluent liquid to a stripping operation to remove any liberated gases therefrom and thereby leaving an aqueous sodium sulfate containing solution; and d. subjecting said resulting aqueous sodium sulfate containing solution to an electrolytic process treatment whereby aqueous sulfuric acid or an aqueous mixture of sulfuric acid and sodium sulfate is collected at the anode and is recycled for utilization in the aforesaid reaction step and aqueous sodium hydroxide which forms at the cathode is collected and recycled for use in the sodium hydroxide treatment step, the improvement which comprises treating the effluent from the alkali metal hydroxide treatment of step (a) to remove substantially all organic impurities therefrom.
Claim 3
Dependent Claim 15 words
The process according to claim 1 wherein said aqueous sodium hydroxide solution contains sodium sulfate.
Claim 4
Dependent Claim 18 words
The process according to claim 1 wherein said sodium hydroxide which forms at the cathode contains sodium sulfate.
Claim 5
Dependent Claim 33 words
The process according to claim 1 wherein to the cathode compartment involved in the electrolytic process is added aqueous sodium sulfate in an amount sufficient to maintain the electrolytic membrane free from solids.
Claim 6
Dependent Claim 17 words
The process according to claim 1 wherein said effluent liquid contains a small amount of sodium hydroxide.
Claim 7
Dependent Claim 16 words
The process according to claim 1 wherein said effluent liquid contains sodium bisulfide and/or sodium bicarbonate.
Claim 8
Dependent Claim 22 words
The process according to claim 1 wherein the effluent liquid from sodium hydroxide contacting is extracted with a substantially water-immiscible organic solvent.
Claim 9
Dependent Claim 25 words
The process according to claim 7 wherein said organic solvent is a hydrocarbon having a boiling point no higher than that of a gas oil.
Claim 10
Dependent Claim 13 words
The process according to claim 8 wherein said hydrocarbon solvent is a naphtha.
Claim 11
Dependent Claim 14 words
The process according to claim 8 wherein said hydrocarbon solvent is a gas oil.
Claim 12
Dependent Claim 19 words
The process according to claim 1 wherein said effluent liquid from sodium hydroxide contacting is contacted with an adsorbent.
Claim 13
Dependent Claim 24 words
The process according to claim 1 wherein said sodium hydroxide treatment step consists of contacting said gas substantially countercurrently with said sodium hydroxide solution.
Claim 14
Dependent Claim 22 words
The process according to claim 1 wherein the liberated gases from the stripping operation include hydrogen sulfide which is converted to sulfur.
Claim 15
Dependent Claim 25 words
The process according to claim 1 wherein the aqueous sodium sulfate from the stripping operation is filtered before it is subjected to the electrolytic process.
Claim 16
Dependent Claim 32 words
The process according to claim 1 wherein said electrolytic process is carried out in an electrolytic cell capable of converting soluble alkali metal salts into their corresponding alkali metal hydroxides and acids.
Claim 17
Dependent Claim 24 words
The process according to claim 15 wherein said soluble alkali metal salt is sodium sulfate which is converted to sodium hydroxide and sulfuric acid.
Claim 18
Dependent Claim 56 words
The process according to claim 15 wherein said electrolytic cell is a three compartment cell comprising a cathode compartment, a center compartment and an anode compartment, the cathode compartment being separated from the center compartment by a cation selective ion exchange membrane and the center compartment being separated from the anode compartment by a fluid-permeable diaphram.

References Cited (Backward Citations)

US1132697A Cited
US2497954A Cited
US3344050A Cited
US3475122A Cited
US3660016A Cited
US3523880A Cited
US3801698A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1980-08-08 1981-02-07 1981-08-09 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1984-08-08 1985-02-07 1985-08-09 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1988-08-08 1989-02-07 1989-08-09 $7700.00 Window Closed / Lapsed

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