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US4044114A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for purifying a gas containing sulfur compounds

Assignee: IFP Energies nouvelles
•
Filing: 1975-12-16
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Granted: 1977-08-23
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Expires: 1995-12-16
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Abstract

Abstract Process for purifying a gas containing hydrogen sulfide and sulfur dioxide, comprising substantially removing sulfur dioxide, absorbing hydrogen sulfide on a solid contact mass, intermittently regenerating said mass by means of an oxygen-containing gas, so as to produce a gas containing sulfur dioxide, and reacting the latter gas with hydrogen sulfide to produce sulfur.

Inventors

  • 👤 Claude Dezael
  • 👤 Sigismond Franckowiak
  • 👤 Philippe Courty
  • 👤 Henri Gruhier

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 17:51
CPC Classifications
C; C01; C01B; C01B17/00; C01B17/02; C01B17/04; C01B17/05; B; B01; B01D; B01D53/00; B01D53/34; B01D53/74; B01D53/86; B01D53/8603; B01D53/8612; B01D53/8615; C01B17/0404; C01B17/0408; C01B17/0456

Claims Analysis

Total Claims: 8
Claim 1
Independent Claim 206 words
A process for purifying a gas containing hydrogen sulfide and sulfur dioxide in a molar ratio of H 2 S to SO 2 of more than 2 : 1, said gas being discharged from a sulfur production unit in which hydrogen sulfide is oxidized by means of molecular oxygen or sulfur dioxide in gas phase, comprising the steps of (a) contacting the hydrogen sulfide and sulfur dioxide containing gas with molten sulfur or with an organic solvent, thereby producing sulfur by reaction between said hydrogen sulfide and said sulfur dioxide, and recovering separately said produced sulfur and a gas of relatively higher H 2 S to SO 2 molar ratio, (b) passing the gas recovered from step (a) over a solid zinc oxide containing mass at 300°-800° C. for absorbing hydrogen sulfide and discharging the resultant H 2 S depleted gas, (c) periodically interrupting the contact of the gas with said mass and passing over the same at 400°-1200° C. a gas containing molecular oxygen produced by burning hydrogen sulfide with an excess oxygen containing gas, thereby regenerating the mass, and recovering an SO 2 containing effluent gas, and (d) reacting said effluent gas with hydrogen sulfide in said sulfur production unit thereby producing additional sulfur.
Claim 2
Dependent Claim 206 words
A process for purifying a gas containing hydrogen sulfide and sulfur dioxide in a molar ratio of H 2 S to SO 2 of more than 2 : 1, said gas being discharged from a sulfur production unit in which hydrogen sulfide is oxidized by means of molecular oxygen or sulfur dioxide in gas phase, comprising the steps of (a) contacting the hydrogen sulfide and sulfur dioxide containing gas with molten sulfur or with an organic solvent, thereby producing sulfur by reaction between said hydrogen sulfide and said sulfur dioxide, and recovering separately said produced sulfur and a gas of relatively higher H 2 S to SO 2 molar ratio, (b) passing the gas recovered from step (a) over a solid zinc oxide containing mass at 300°-800° C. for absorbing hydrogen sulfide and discharging the resultant H 2 S depleted gas, (c) periodically interrupting the contact of the gas with said mass and passing over the same at 400°-1200° C. a gas containing molecular oxygen produced by burning hydrogen sulfide with an excess oxygen containing gas, thereby regenerating the mass, and recovering an SO 2 containing effluent gas, and (d) reacting said effluent gas with hydrogen sulfide in said sulfur production unit thereby producing additional sulfur.
Claim 3
Dependent Claim 43 words
A process according to claim 1, in which the mass for absorbing hydrogen sulfide contains by weight from 20 to 90% of a zinc oxide, from 0.9 to 50% of alumina and from 2 to 45% of a group II A metal oxide.
Claim 4
Dependent Claim 45 words
A process according to claim 2, in which the mass further contains from 1 to 20% by weight of an oxide of at least one metal selected from the group consisting of copper, cadmium, titanium, zirconium, vanadium, chromium, molybdenum, tungsten, manganese, iron, cobalt and nickel.
Claim 5
Dependent Claim 19 words
A process according to claim 2, in which the zinc oxide content is from 25 to 80% by weight.
Claim 6
Dependent Claim 20 words
A process according to claim 1, in which the gas to be purified also contains carbon oxysulfide and/or carbon sulfide.
Claim 7
Dependent Claim 66 words
A process according to claim 1, wherein the zinc oxide containing mass analyzes by weight 20-85% of zinc oxide, 0.9-50% of alumina, 2-45% of a group II A metal oxide, and at least 50% of said group IIA metal oxide is combined with alumina as metal IIA aluminate or silicoaluminate and at least the major portion of said zinc oxide is present as the free oxide.
Claim 8
Dependent Claim 47 words
A process according to claim 1, wherein said zinc oxide containing mass results from admixing a zinc compound with a refractory cement analyzing 40-85% by weight of alumina and 10-40% by weight of oxide of a group IIA metal and then heating the mixture to 500°-1,000° C.

References Cited (Backward Citations)

US1915364A Cited
US2747968A Cited
US3812243A Cited
US3845197A Cited
US3848071A Cited
US3896215A Cited
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USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1980-08-22 1981-02-21 1981-08-23 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1984-08-22 1985-02-21 1985-08-23 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1988-08-22 1989-02-21 1989-08-23 $7700.00 Window Closed / Lapsed

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