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US4008174A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for regenerating a solid copper-chromium reactant used in the removal of hydrogen sulfide from hydrogen recycle gas

Assignee: Chevron USA Inc
•
Filing: 1976-01-19
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Granted: 1977-02-15
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Expires: 1996-01-19
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Abstract

Abstract A process is disclosed for regenerating a solid reactant comprising a copper component and a chromium component disposed on a porous carbon support when the reactant has been expended by reaction with hydrogen sulfide contained in hydrogen recycle gas in a hydrocarbon reforming system, regeneration being accomplished by: (a) contacting the expended solid reactant with dilute oxygen in an inert diluent gas at a temperature in the range from 200° to 425° F; (b) contacting the solid material from step (a) with hydrogen at a temperature in the range from 300° to 500° F; and (c) contacting the solid material resulting from step (b) with an inert gas at a temperature in the range from 400° to 600° F.

Inventors

  • 👤 Robert L. Jacobson
  • 👤 Kirk R. Gibson

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-30 00:21
CPC Classifications
A; A01; A01N; A01N37/00; A01N37/36; A01N37/38; A01N37/40; B; B01; B01D; B01D53/00; B01D53/34; B01D53/46; B01D53/48; B01D53/52; B01J; B01J20/00; B01J20/02; B01J20/0203; B01J20/0218; B01J20/0233; B01J20/0237; B01J20/20; B01J20/28; B01J20/28054; B01J20/28057; B01J20/30; B01J20/32; B01J20/3202; B01J20/3204; B01J20/3231; B01J20/3234; B01J20/3236; B01J20/34; B01J20/3416; B01J20/3483; C; C01; C01B; C01B17/00; C01B17/48; C01B17/50; C01B17/60; C09; C09D; C09D5/00; C09D5/16; C09D5/1606; C09D5/1612; C09D5/1625; C10; C10G; C10G35/00; C10G35/04; C10G35/06; C10G35/085; Y; Y10; Y10S; Y10S502/00; Y10S502/515; Y10S502/517

Claims Analysis

Total Claims: 6
Claim 1
Independent Claim 200 words
A process for regenerating a solid reactant comprising copper and chromium disposed on a high-surface-area carbon support, said reactant having reacted to form a solid sulfur compound by contact with a hydrogen sulfide-containing recycle hydrogen stream in a hydrocarbon reforming system for removing substantially all the hydrogen sulfide from said hydrogen stream, said regeneration process comprising the steps of: a. forming sulfate by reacting said sulfur compound with oxygen in an oxygen-containing gas comprising an inert gas and about 0.1 to about 2 weight percent oxygen at a temperature between about 200° F and 425° F, whereby reduction of the surface area of said carbon support is prevented, and removing the resulting gas from contact with the resulting solid; b. forming sulfur dioxide by reacting said sulfate with hydrogen at a temperature of about 300° F to about 500° F, whereby a portion of the sulfur dioxide is adsorbed on said resulting solid, and removing the resulting gas from contact with said resulting solid; and c. desorbing sulfur dioxide from said resulting solid by contacting said solid with an inert gas at a temperature of 450° F to 600° F and removing the resulting gas from contact with said solid.
Claim 2
Dependent Claim 200 words
A process for regenerating a solid reactant comprising copper and chromium disposed on a high-surface-area carbon support, said reactant having reacted to form a solid sulfur compound by contact with a hydrogen sulfide-containing recycle hydrogen stream in a hydrocarbon reforming system for removing substantially all the hydrogen sulfide from said hydrogen stream, said regeneration process comprising the steps of: a. forming sulfate by reacting said sulfur compound with oxygen in an oxygen-containing gas comprising an inert gas and about 0.1 to about 2 weight percent oxygen at a temperature between about 200° F and 425° F, whereby reduction of the surface area of said carbon support is prevented, and removing the resulting gas from contact with the resulting solid; b. forming sulfur dioxide by reacting said sulfate with hydrogen at a temperature of about 300° F to about 500° F, whereby a portion of the sulfur dioxide is adsorbed on said resulting solid, and removing the resulting gas from contact with said resulting solid; and c. desorbing sulfur dioxide from said resulting solid by contacting said solid with an inert gas at a temperature of 450° F to 600° F and removing the resulting gas from contact with said solid.
Claim 3
Dependent Claim 25 words
A process according to claim 1 wherein said expended reactant is contacted with said oxygen-containing gas at a temperature between 350° F and 400° F.
Claim 4
Dependent Claim 26 words
A process according to claim 1 wherein said resulting solid from step (a) is contacted with hydrogen at a temperature between 350° F and 400° F.
Claim 5
Dependent Claim 28 words
A process according to claim 1 wherein said resulting solid from step (b) is contacted with an inert gas at a temperature between 450° F and 550° F.
Claim 6
Dependent Claim 36 words
A process according to claim 1 wherein said solid reactant contains between 7.8 and 16 weight percent of said copper component and between 1.7 and 4 weight percent of said chromium component, on an elemental-metal basis.

References Cited (Backward Citations)

US1947776A Cited
US2747968A Cited
US3576596A Cited
US3883637A Cited
US3778501A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1980-02-15 1980-08-16 1981-02-15 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1984-02-15 1984-08-16 1985-02-15 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1988-02-15 1988-08-16 1989-02-15 $7700.00 Window Closed / Lapsed

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