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US4192857A Expired / Lapsed US ⏱️ 0.0 years remaining

Sulphur production

Assignee: Societe Nationale Elf Aquitaine Production SA
•
Filing: 1977-11-14
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Granted: 1980-03-11
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Expires: 1997-11-14
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Abstract

Abstract The Claus process for the production of sulphur is improved by employing a deoxidation catalyst prior to the conventional Claus oxide catalyst.

Inventors

  • 👤 Jacques Tellier
  • 👤 Andre Philippe
  • 👤 Pierre Mathieu
  • 👤 Robert Voirin

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-30 13:24
CPC Classifications
B; B01; B01J; B01J35/00; B01J35/60; C; C01; C01B; C01B17/00; C01B17/02; C01B17/04; C01B17/0404; C01B17/0426; B01J35/61; B01J35/615; B01J35/63; B01J35/633

Claims Analysis

Total Claims: 12
Claim 1
Independent Claim 159 words
A Claus process for the production of sulphur by the action of H 2 S on SO 2 in the presence of an oxide catalyst which comprises contacting a gas containing H 2 S and SO 2 and 50-5000 vpm O 2 in at least one catalytic reaction zone containing a deoxidation catalyst and a Claus oxide catalyst such that said gas encounters for 0.1-3 seconds NTP the deoxidation catalyst prior to encountering the Claus oxide catalyst, said deoxidation catalyst consisting of a supported metal compound of at least one metal selected from the group consisting of iron, nickel, cobalt, copper and zinc, the support having a surface area of at least 100 m 2 /g and a porosity of at least 0.2 ml/g, said deoxidation catalyst containing about 0.5-10% by weight of metal relative to the Claus oxide catalyst, whereby the magnitude of said Claus catalyst activity degradation with time is retarded by use of said deoxidation catalyst.
Claim 2
Dependent Claim 159 words
A Claus process for the production of sulphur by the action of H 2 S on SO 2 in the presence of an oxide catalyst which comprises contacting a gas containing H 2 S and SO 2 and 50-5000 vpm O 2 in at least one catalytic reaction zone containing a deoxidation catalyst and a Claus oxide catalyst such that said gas encounters for 0.1-3 seconds NTP the deoxidation catalyst prior to encountering the Claus oxide catalyst, said deoxidation catalyst consisting of a supported metal compound of at least one metal selected from the group consisting of iron, nickel, cobalt, copper and zinc, the support having a surface area of at least 100 m 2 /g and a porosity of at least 0.2 ml/g, said deoxidation catalyst containing about 0.5-10% by weight of metal relative to the Claus oxide catalyst, whereby the magnitude of said Claus catalyst activity degradation with time is retarded by use of said deoxidation catalyst.
Claim 3
Dependent Claim 20 words
A process as claimed in claim 1, characterised in that the metal compound of the deoxidation catalyst is iron sulphate.
Claim 4
Dependent Claim 15 words
A process as claimed in claim 1, characterised in that the support is a silico-aluminate.
Claim 5
Dependent Claim 29 words
A process as claimed in one of claims 1, characterised in that the deoxidation catalyst and the oxide catalyst are used at temperatures below the dewpoint of the sulphur.
Claim 6
Dependent Claim 28 words
A process as claimed in claim 4, characterised in that the deoxidation catalyst is periodically desulphurised by a gas containing H 2 S between 250° and 400° C.
Claim 7
Dependent Claim 27 words
A process as claimed in claim 1 characterised in that the volume of deoxidation catalyst is about 5 to 50% of the volume of the oxide catalyst.
Claim 8
Dependent Claim 53 words
A process as claimed in claim 1 characterised in that in addition to the main sulphur compounds in the form of H 2 S and SO 2 , the gas to be processed also contains secondary sulphur compounds in the form of COS and CS 2 in concentrations less than 5% by volume.
Claim 9
Dependent Claim 37 words
A process as claimed in claim 1 wherein the support has a surface area greater than 150 m 2 /g and wherein the weight of said metal is 2-6% of the weight of said Claus oxide catalyst.
Claim 10
Dependent Claim 27 words
A process as claimed in claim 6 characterized in that the volume of the deoxidation catalyst is 10 to 40% of the volume of the oxide catalyst.
Claim 11
Dependent Claim 19 words
A process as claimed in claim 1 characterized in that the deoxidation catalyst and the oxide catalyst are superposed.
Claim 12
Dependent Claim 37 words
A process as claimed in claim 8 characterized in that the volume of the deoxidation catalyst is 10 to 40% of the volume of the oxide catalyst, and the deoxidation catalyst is ferrous oxide supported on alumina.

References Cited (Backward Citations)

GB189613844A Cited
GB524345A Cited
US2787519A Cited
US3554689A Cited
US3725531A Cited
US3939250A Cited
US3978004A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1983-03-11 1983-09-10 1984-03-11 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1987-03-11 1987-09-10 1988-03-11 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1991-03-11 1991-09-10 1992-03-11 $7700.00 Window Closed / Lapsed

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