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US4377495A Expired / Lapsed US ⏱️ 0.0 years remaining

Regeneration of sulfur-contaminated platinum-alumina catalyst

Assignee: BASF Catalysts LLC
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Filing: 1982-03-11
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Granted: 1983-03-22
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Expires: 2002-03-11
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Abstract

Abstract Platinum-alumina catalysts deactivated by accumulations of sulfur and carbonaceous deposits are treated for removal of sulfur by contacting the deactivated catalyst with a hydrogen-rich gas, water or water precursor, a solution of liquid chlorinated hydrocarbon containing one to eight carbon atoms per molecule, in an oxygen-containing organic compound containing one to eight carbon atoms per molecule prior to contacting the deactivated catalyst with oxygen-containing regeneration gas for removal of coke deposits from the catalyst.

Inventors

  • 👤 Harold F. Tse

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-03 03:20
CPC Classifications
B; B01; B01J; B01J23/00; B01J23/90; B01J23/96; C; C10; C10G; C10G35/00; C10G35/04; C10G35/06; C10G35/085; C10G35/09

Claims Analysis

Total Claims: 11
Claim 1
Independent Claim 236 words
In a method of regenerating a deactivated sulfur-containing hydrocarbon conversion catalyst comprising platinum on an alumina support by burning coke from said catalyst with an oxygen-containing gas wherein sulfur is removed from said catalyst prior to burning coke therefrom by contacting said deactivated catalyst at an elevated temperature in the range of 350° to 600° C. with a hydrogen-rich gas comprising liquid or gaseous water and a chlorine compound, the improvement which comprises removing sulfur from said catalyst by contacting said deactivated catalyst at said elevated temperature with a hydrogen-rich gas containing liquid or gaseous water and an oxygen-containing organic compound containing one to eight carbon atoms per molecule and selected from the class consisting of hydroxylated compounds, ketones and ethers and having dissolved therein a chlorinated hydrocarbon containing one to eight carbon atoms per molecule in relative proportions in the range of 5 to 100 volumes of said oxygen-containing organic compound for each volume of said chlorinated hydrocarbon, and maintaining the rate of addition of said oxygen-containing organic compound and said chlorinated hydrocarbon dissolved therein such that the relative proportions of water and said chlorinated hydrocarbon are in the range of about 20 to about 80 mols of water per atomic equivalent of chlorine, withdrawing from said zone an effluent gas stream containing hydrogen sulfide, and continuing said process until the hydrogen sulfide content of said effluent gas stream is reduced to a desired concentration.
Claim 2
Dependent Claim 236 words
In a method of regenerating a deactivated sulfur-containing hydrocarbon conversion catalyst comprising platinum on an alumina support by burning coke from said catalyst with an oxygen-containing gas wherein sulfur is removed from said catalyst prior to burning coke therefrom by contacting said deactivated catalyst at an elevated temperature in the range of 350° to 600° C. with a hydrogen-rich gas comprising liquid or gaseous water and a chlorine compound, the improvement which comprises removing sulfur from said catalyst by contacting said deactivated catalyst at said elevated temperature with a hydrogen-rich gas containing liquid or gaseous water and an oxygen-containing organic compound containing one to eight carbon atoms per molecule and selected from the class consisting of hydroxylated compounds, ketones and ethers and having dissolved therein a chlorinated hydrocarbon containing one to eight carbon atoms per molecule in relative proportions in the range of 5 to 100 volumes of said oxygen-containing organic compound for each volume of said chlorinated hydrocarbon, and maintaining the rate of addition of said oxygen-containing organic compound and said chlorinated hydrocarbon dissolved therein such that the relative proportions of water and said chlorinated hydrocarbon are in the range of about 20 to about 80 mols of water per atomic equivalent of chlorine, withdrawing from said zone an effluent gas stream containing hydrogen sulfide, and continuing said process until the hydrogen sulfide content of said effluent gas stream is reduced to a desired concentration.
Claim 3
Dependent Claim 13 words
The method according to claim 1 wherein said oxygen-containing compound is an alkanol.
Claim 4
Dependent Claim 12 words
The method according to claim 1 wherein said oxygen-containing compound is methanol.
Claim 5
Dependent Claim 12 words
The method according to claim 1 wherein said oxygen-containing compound is isopropanol.
Claim 6
Dependent Claim 13 words
The process of claim 1 wherein said oxygen-containing compound is methyl ethyl ketone.
Claim 7
Dependent Claim 17 words
The process of claim 1 wherein said chlorinated hydrocarbon contains one to four carbon atoms per molecule.
Claim 8
Dependent Claim 12 words
The process of claim 1 wherein said chlorinated hydrocarbon is carbon tetrachloride.
Claim 9
Dependent Claim 17 words
The process of claim 1 wherein said hydrogen-rich gas is recycle gas from the hydrocarbon conversion process.
Claim 10
Dependent Claim 13 words
The process of claim 1 wherein said catalyst is a naphtha reforming catalyst.
Claim 11
Dependent Claim 26 words
The process of claim 1 wherein the sulfur removal step is carried out at a temperature within the range of about 425° to about 540° C.

References Cited (Backward Citations)

US3673109A Cited
US3622520A Cited
US3935244A Cited
US4155836A Cited
US4191633A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1986-03-21 1986-09-20 1987-03-22 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1990-03-21 1990-09-20 1991-03-22 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1994-03-21 1994-09-20 1995-03-22 $7700.00 Window Closed / Lapsed

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