US4287051A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Disposition of a high nitrogen content oil stream
Assignee: Atlantic Richfield Co
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Filing: 1979-11-08
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Granted: 1981-09-01
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Expires: 1999-11-08
Abstract
Abstract A method of denitrogenating viscous oils containing a relatively high content of nitrogenous compounds and of disposing of a resulting high nitrogen content oil stream, characterized by forming a raw oil stream and a first viscous bottoms stream that would not be operably pumpable to a partial oxidation unit without the inclusion of viscosity lowering constituents; extracting the nitrogenous compounds from the raw oil stream with an operable acid solvent to produce a raffinate oil of low nitrogen content oil and an extract stream of low viscosity, high nitrogen content oil; recovering the acid solvent from the extract stream, simultaneously producing a small volume stream of low viscosity, high nitrogen content oil; admixing the low viscosity high nitrogen content oil with the high viscosity bottoms stream to provide a pumpable mixed stream; sending the mixed stream to a partial oxidation unit to produce hydrogen; employing the produced hydrogen for hydrogenation of the raffinate oil at mild conditions; and recycling the acid solvent to the extraction step. Additional and alternative steps are also disclosed.
Inventors
- 👤 Daniel J. Curtin
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-05 12:05
CPC Classifications
C; C10; C10G; C10G67/00; C10G67/02; C10G67/08; C10G1/00; C10G1/002
Claims Analysis
Total Claims: 12
Claim 1
Independent Claim
251 words
A method of denitrogenating a viscous oil containing a relatively high content of nitrogenous compounds and of disposing of the extract oil stream containing a high concentration of the nitrogenous compounds extracted, comprising: a. forming a first portion and a remaining portion of the viscous oil stream; said remaining portion comprising a first viscous bottom stream that would not be operably pumpable to a partial oxidation unit without the inclusion of viscosity lowering constitutents; b. extracting the nitrogenous compounds from said first portion of the viscous oil with an operable acid solvent to produce a raffinate oil having a relatively low concentration of nitrogenous compounds such that said raffinate oil can be hydrodenitrogenated at mild conditions with reduced hydrogen consumption; and an extract stream of high content of nitrogenous compounds; c. recovering the acid solvent from said extract stream, simultaneously producing a small volume stream of low viscosity oil containing a high concentration of nitrogenous compounds and referred to as a high nitrogen content oil; d. admixing said low viscosity high nitrogen content oil with the remaining portion of said viscous oil comprising said first viscous bottoms stream to provide a pumpable mixed stream; e. sending said mixed stream to a partial oxidation unit where hydrogen is produced; f. employing the hydrogen produced in step e to effect hydrodenitrogenation of the raffinate oil by hydrogenating the raffinate oil at mild conditions to produce an ultimate product oil stream; and g. recycling said acid solvent to the extracting operation of step b.
Claim 2
Independent Claim
251 words
A method of denitrogenating a viscous oil containing a relatively high content of nitrogenous compounds and of disposing of the extract oil stream containing a high concentration of the nitrogenous compounds extracted, comprising: a. forming a first portion and a remaining portion of the viscous oil stream; said remaining portion comprising a first viscous bottom stream that would not be operably pumpable to a partial oxidation unit without the inclusion of viscosity lowering constitutents; b. extracting the nitrogenous compounds from said first portion of the viscous oil with an operable acid solvent to produce a raffinate oil having a relatively low concentration of nitrogenous compounds such that said raffinate oil can be hydrodenitrogenated at mild conditions with reduced hydrogen consumption; and an extract stream of high content of nitrogenous compounds; c. recovering the acid solvent from said extract stream, simultaneously producing a small volume stream of low viscosity oil containing a high concentration of nitrogenous compounds and referred to as a high nitrogen content oil; d. admixing said low viscosity high nitrogen content oil with the remaining portion of said viscous oil comprising said first viscous bottoms stream to provide a pumpable mixed stream; e. sending said mixed stream to a partial oxidation unit where hydrogen is produced; f. employing the hydrogen produced in step e to effect hydrodenitrogenation of the raffinate oil by hydrogenating the raffinate oil at mild conditions to produce an ultimate product oil stream; and g. recycling said acid solvent to the extracting operation of step b.
Claim 3
Dependent Claim
26 words
The method of claim 1 wherein said oil is subjected to hydrogenation to lower the concentration of the nitrogenous compounds before the extracting of step b.
Claim 4
Dependent Claim
27 words
The method of claim 1 wherein said acid solvent is selected from the class consisting of phosphoric acid, formic acid, and a monoammonium salt of phosphoric acid.
Claim 5
Dependent Claim
12 words
The method of claim 3 wherein said acid solvent comprises formic acid.
Claim 6
Dependent Claim
26 words
The method of claim 1 wherein said acid solvent recovery is by distillation of the bottoms into respective acid solvent and high nitrogen content oil streams.
Claim 7
Dependent Claim
13 words
The method of claim 1 wherein said acid solvent recovery is by neutralization.
Claim 8
Dependent Claim
57 words
The method of claim 6 wherein said neutralization is with ammonium hydroxide and produces an extract oil that is washed and the bottom wash is combined with the bottoms from the neutralization to produce a solution from which the acid solvent is recovered and recycled, simultaneously producing ammonium hydroxide which is also recycled to the neutralizing reactor.
Claim 9
Dependent Claim
27 words
The method of claim 1 wherein said high nitrogen content oil stream is washed with water before being sent onto its destination in accordance with step c.
Claim 10
Dependent Claim
24 words
The method of claim 1 wherein said raffinate oil having low concentration of nitrogenous compounds is washed with water before being sent to hydronitrogenation.
Claim 11
Dependent Claim
48 words
The method of claim 1 wherein said raffinate oil is sent to a mild hydrodenitrogenation unit where the nitrogenous compounds are converted to ammonia and the sulfur compounds are converted to H 2 S and said ammonia and H 2 S are removed from the product oil stream.
Claim 12
Dependent Claim
61 words
The method of claim 1 wherein said oil also contains sulfurous contaminants as well as the nitrogenous contaminants and said nitrogenous and sulfurous contaminants are converted to ammonia and hydrogen sulfide in the partial oxidation unit and the ammonia and hydrogen sulfide are recovered separately from said hydrogen to alleviate difficulties with said ammonia and hydrogen sulfide in the effluent streams.
References Cited (Backward Citations)
US2263175A
Cited
US2309324A
Cited
US2541458A
Cited
US2704758A
Cited
US2662843A
Cited
US3380910A
Cited
US3537977A
Cited
US3523071A
Cited
US4115246A
Cited
US4159940A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1984-08-31 | 1985-03-02 | 1985-09-01 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1988-08-31 | 1989-03-02 | 1989-09-01 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1992-08-31 | 1993-03-02 | 1993-09-01 | $7700.00 | Window Closed / Lapsed |