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US4798716A Expired / Lapsed US ⏱️ 0.0 years remaining

Sulfur recovery plant and process using oxygen

Assignee: BP Corp North America Inc
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Filing: 1987-12-07
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Granted: 1989-01-17
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Expires: 2007-12-07
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Abstract

Abstract Oxygen enriched gas to Claus furnace or catalytic reactor is diluted with a process derived dilute H 2 S or SO 2 stream to prevent excessive temperature rise due to use of the oxygen enriched gas.

Inventors

  • 👤 John W. Palm

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 11:43
CPC Classifications
C; C01; C01B; C01B17/00; C01B17/02; C01B17/04; C01B17/0404; C01B17/0413

Claims Analysis

Total Claims: 7
Claim 1
Independent Claim 239 words
Process for the recovery of sulfur from a gaseous stream containing hydrogen sulfide, said process comprising the steps of: (a) introducing a thermal reaction mixture comprising (1) said gaseous stream containing hydrogen sulfide, and (2) an oxygen-enriched stream of air or pure oxygen into a combustion zone of a Claus furnace; (b) combusting said thermal reaction mixture in said Claus furnace to thereby produce hot combustion gases comprising hydrogen sulfide, sulfur dioxide, carbon dioxide, water, and elemental sulfur; (c) introducing said hot combustion gases into a Claus catalytic reactor; (d) subjecting said hot combustion gases in said catalytic reactor to Claus reaction conditions in the presence of a Claus catalyst to thereby produce a Claus plant gaseous effluent stream comprising hydrogen sulfide, sulfur dioxide, carbon dioxide, water, and elemental sulfur; (e) introducing said Claus plant gaseous effluent into a condenser to thereby produce liquid sulfur, which is recovered, and a gaseous condenser effluent, which comprises hydrogen sulfide, sulfur dioxide, carbon dioxide and water; (f) converting substantially all sulfur species in said gaseous condenser effluent to hydrogen sulfide, to thereby form a condenser effluent comprising hydrogen sulfide, carbon dioxide and water; (g) removing water form the condenser effluent from step (f); and (h) moderating the temperature in said Claus furnace by returning at least a portion of the dried condenser effluent from step (g), as a diluent stream, to a combustion zone of the Claus furnace in step (a) above.
Claim 2
Dependent Claim 239 words
Process for the recovery of sulfur from a gaseous stream containing hydrogen sulfide, said process comprising the steps of: (a) introducing a thermal reaction mixture comprising (1) said gaseous stream containing hydrogen sulfide, and (2) an oxygen-enriched stream of air or pure oxygen into a combustion zone of a Claus furnace; (b) combusting said thermal reaction mixture in said Claus furnace to thereby produce hot combustion gases comprising hydrogen sulfide, sulfur dioxide, carbon dioxide, water, and elemental sulfur; (c) introducing said hot combustion gases into a Claus catalytic reactor; (d) subjecting said hot combustion gases in said catalytic reactor to Claus reaction conditions in the presence of a Claus catalyst to thereby produce a Claus plant gaseous effluent stream comprising hydrogen sulfide, sulfur dioxide, carbon dioxide, water, and elemental sulfur; (e) introducing said Claus plant gaseous effluent into a condenser to thereby produce liquid sulfur, which is recovered, and a gaseous condenser effluent, which comprises hydrogen sulfide, sulfur dioxide, carbon dioxide and water; (f) converting substantially all sulfur species in said gaseous condenser effluent to hydrogen sulfide, to thereby form a condenser effluent comprising hydrogen sulfide, carbon dioxide and water; (g) removing water form the condenser effluent from step (f); and (h) moderating the temperature in said Claus furnace by returning at least a portion of the dried condenser effluent from step (g), as a diluent stream, to a combustion zone of the Claus furnace in step (a) above.
Claim 3
Dependent Claim 26 words
Process as in claim 1 wherein, in the absence of providing the diluent stream, temperature of the combustion zone are in excess of about 2600° F.
Claim 4
Dependent Claim 28 words
Process as in claim 1 wherein the ratio of total moles of diluent to moles of O 2 is in the range of about 1:10 to about 10:1.
Claim 5
Dependent Claim 28 words
Process as in claim 1 wherein the ratio of total moles of diluent to moles of O 2 is in the range of about 1:1 to about 6:1.
Claim 6
Dependent Claim 63 words
Process as in claim 1 further comprising: removing a stream of water from step (g) of claim 1 to a sour water stripper and producing a purified water stream and a gaseous second single sulfur species stream; and combining the gaseous second single sulfur species stream with the single sulfur species stream from which water is removed in step (g) of claim 1.
Claim 7
Dependent Claim 51 words
Process as in claim 1 where water is removed from the condenser effluent in step (g) by contacting said condenser effluent with an aqueous stream under conditions such that water in the gaseous condenser effluent is condensed to a liquid and separated from the remaining gaseous components in said condenser effluent.

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1992-01-17 1992-07-18 1993-01-17 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1996-01-17 1996-07-18 1997-01-17 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2000-01-17 2000-07-18 2001-01-17 $7700.00 Window Closed / Lapsed

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