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US4113607A Expired / Lapsed US ⏱️ 0.0 years remaining

Denitrification process for hydrogenated distillate oils

Assignee: Chevron USA Inc
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Filing: 1977-03-03
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Granted: 1978-09-12
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Expires: 1997-03-03
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Abstract

Abstract A process is disclosed for upgrading a hydrogenated distillate oil by extracting nitrogen compounds from the oil. In the process, these compounds are selectively extracted from the oil in a liquid-liquid extraction using as the extracting medium a solution of ferric chloride in furfural. Following intimate contacting of the oil with the extracting solution, the resulting mixture is separated into an oily raffinate phase and a solvent-extract phase. The raffinate oil is especially suitable as a feedstock for a catalytic cracking or hydroprocessing stage employing an acidic catalyst. The extraction is carried out under moderate conditions of temperature and pressure.

Inventors

  • 👤 Stephen J. Miller

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-04 20:33
CPC Classifications
C; C10; C10G; C10G21/00; C10G21/06; C10G29/00; C10G29/06; C10G29/12; C10G67/00; C10G67/02; C10G67/04

Claims Analysis

Total Claims: 11
Claim 1
Independent Claim 136 words
A process for upgrading a hydrogenated distillate oil containing a residual nitrogenous component in an amount, calculated as nitrogen, in the range of from about 10 to 600 ppmw, comprising: (1) extracting a major portion of said component from said oil using a solution of ferric chloride, said extracting being under conditions including (a) a temperature in the range of from about 0° to 50° C and (b) a solution-to-oil volume ratio in the range of from about 0.1 to 5, said solution containing at least a major portion of furfural as the solvent thereof and containing said ferric chloride therein in the range of from about 0.001 to 10 weight percent thereby forming a raffinate oil phase containing a minor portion of said nitrogenous component; and (2) withdrawing said raffinate oil phase from step (1).
Claim 2
Dependent Claim 136 words
A process for upgrading a hydrogenated distillate oil containing a residual nitrogenous component in an amount, calculated as nitrogen, in the range of from about 10 to 600 ppmw, comprising: (1) extracting a major portion of said component from said oil using a solution of ferric chloride, said extracting being under conditions including (a) a temperature in the range of from about 0° to 50° C and (b) a solution-to-oil volume ratio in the range of from about 0.1 to 5, said solution containing at least a major portion of furfural as the solvent thereof and containing said ferric chloride therein in the range of from about 0.001 to 10 weight percent thereby forming a raffinate oil phase containing a minor portion of said nitrogenous component; and (2) withdrawing said raffinate oil phase from step (1).
Claim 3
Dependent Claim 35 words
A process as in claim 1 wherein at said withdrawing step (2) the temperature of said phases is below said contacting temperature by an amount in the range of from about 5° to 25° C.
Claim 4
Dependent Claim 38 words
A process as in claim 1 wherein said volume ratio is in the range of from about 0.1 to 3 and said amount of ferric chloride is in the range of from about 0.01 to 5 weight percent.
Claim 5
Dependent Claim 41 words
A process as in claim 1 wherein said temperature range is 10° to 30° C, said volume ratio range is 0.5 to 1.5 and said amount of ferric chloride is in the range of from about 0.1 to 1 weight percent.
Claim 6
Dependent Claim 18 words
A process as in claim 1 wherein said solution contains at least about 80 volume percent of furfural.
Claim 7
Dependent Claim 13 words
A process as in claim 1 wherein said solvent consists essentially of furfural.
Claim 8
Dependent Claim 23 words
A process as in claim 1 wherein said raffinate oil phase has a residual nitrogenous component content which is below about 10 ppmw.
Claim 9
Dependent Claim 23 words
A process as in claim 1 wherein said raffinate oil phase has a residual nitrogenous component content which is below about 2 ppmw.
Claim 10
Dependent Claim 156 words
A process for removing at least 50 percent of a residual nitrogen component from a hydrogenated hydrocarbon distillate feedstock comprising: (1) extracting a first portion of said nitrogen component from said feedstock in a first counter-current extraction column using as the extracting liquid a first extract produced in a second counter-current extraction column, (2) as hereinafter deliniated recovering from said first column a first raffinate and a second extract; (3) extracting a second portion of said nitrogen component from said first raffinate in said second column using as the extracting liquid a solution of ferric chloride, said solution containing (a) at least a major portion of furfural as the solvent thereof and (b) an amount of ferric chloride in the range of from about 0.001 to 10 weight percent; and (4) recovering from said second column a second raffinate and said first extract, said second raffinate containing not more than 50 percent of said nitrogen component.
Claim 11
Dependent Claim 156 words
A process for removing at least 50 percent of a residual nitrogen component from a hydrogenated hydrocarbon distillate feedstock comprising: (1) extracting a first portion of said nitrogen component from said feedstock in a first counter-current extraction column using as the extracting liquid a first extract produced in a second counter-current extraction column, (2) as hereinafter deliniated recovering from said first column a first raffinate and a second extract; (3) extracting a second portion of said nitrogen component from said first raffinate in said second column using as the extracting liquid a solution of ferric chloride, said solution containing (a) at least a major portion of furfural as the solvent thereof and (b) an amount of ferric chloride in the range of from about 0.001 to 10 weight percent; and (4) recovering from said second column a second raffinate and said first extract, said second raffinate containing not more than 50 percent of said nitrogen component.

References Cited (Backward Citations)

US2507861A Cited
US2847362A Cited
US2846358A Cited
US3193496A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1981-09-11 1982-03-13 1982-09-12 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1985-09-11 1986-03-13 1986-09-12 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1989-09-11 1990-03-13 1990-09-12 $7700.00 Window Closed / Lapsed

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