US4592832A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for increasing Bright Stock raffinate oil production
Assignee: ExxonMobil Technology and Engineering Co
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Filing: 1984-09-06
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Granted: 1986-06-03
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Expires: 2004-09-06
Abstract
Abstract A process for increasing the production of Bright Stock oil in a lube oil process scheme. Aromatic extract oil, after being separated from the extraction solvent, is recycled back to the deasphalter unit and combined with a vacuum residuum in 10-20 LV %, based on the total deasphalter feed, prior to deasphalting. After deasphalting and aromatics extraction the absolute yield of raffinate is increased.
Inventors
- 👤 Duncan J. Bristow
- 👤 Biddanda U. Achia
- 👤 Lawrence J. Evers
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-08 20:01
CPC Classifications
C; C10; C10G; C10G53/00; C10G53/02; C10G53/04; C10G53/06
Claims Analysis
Total Claims: 6
Claim 1
Independent Claim
245 words
In a process for increasing the amount of Bright Stock raffinate oil derived from the solvent extraction of deasphalted lube oil involving the steps of: (a) extracting a vacuum residuum with a low molecular weight alkane hydrocarbon solvent resulting in a deasphalted lube oil solution and asphaltic residue; (b) separating said deasphalted lube oil and said residue; (c) separating said hydrocarbon solvent from said deasphalted lube oil; (d) extracting said deasphalted lube oil obtained from step (c) with an aromatics solvent resulting in a Bright Stock raffinate oil solution and an extract oil solution, said extract oil solution comprised of dissolved aromatics and recoverable raffinate; (e) separating said raffinate solution from said extract oil solution obtained from step (d); and (f) separating said aromatics solvent from said extract oil solution obtained from step (e); in which said improvement comprises the steps of: (g) recycling said extract oil from which the aromatics solvent has been removed, obtained from step (f), to step (a) and combining said extract oil with said vacuum residuum in a 10-20 LV %, based on said residuum, prior to said deasphalting; (h) repeating step (a); (i) repeating step (b); (j) repeating step (c); (k) extracting said deasphalted oil obtained from step (j) with said aromatics solvent resulting in said Bright Stock raffinate oil and said extract oil, wherein said obtained raffinate is present in a substantially greater amount, based on said vacuum residuum, as compared to said raffinate obtained in step (d).
Claim 2
Dependent Claim
245 words
In a process for increasing the amount of Bright Stock raffinate oil derived from the solvent extraction of deasphalted lube oil involving the steps of: (a) extracting a vacuum residuum with a low molecular weight alkane hydrocarbon solvent resulting in a deasphalted lube oil solution and asphaltic residue; (b) separating said deasphalted lube oil and said residue; (c) separating said hydrocarbon solvent from said deasphalted lube oil; (d) extracting said deasphalted lube oil obtained from step (c) with an aromatics solvent resulting in a Bright Stock raffinate oil solution and an extract oil solution, said extract oil solution comprised of dissolved aromatics and recoverable raffinate; (e) separating said raffinate solution from said extract oil solution obtained from step (d); and (f) separating said aromatics solvent from said extract oil solution obtained from step (e); in which said improvement comprises the steps of: (g) recycling said extract oil from which the aromatics solvent has been removed, obtained from step (f), to step (a) and combining said extract oil with said vacuum residuum in a 10-20 LV %, based on said residuum, prior to said deasphalting; (h) repeating step (a); (i) repeating step (b); (j) repeating step (c); (k) extracting said deasphalted oil obtained from step (j) with said aromatics solvent resulting in said Bright Stock raffinate oil and said extract oil, wherein said obtained raffinate is present in a substantially greater amount, based on said vacuum residuum, as compared to said raffinate obtained in step (d).
Claim 3
Dependent Claim
27 words
The process of claim 1 wherein said extract oil is combined with said vacuum residuum in step (g) in about 15 LV % prior to said deasphalting.
Claim 4
Dependent Claim
14 words
The process of claim 1 wherein said hydrocarbon solvent in step (a) is propane.
Claim 5
Dependent Claim
14 words
The process of claim 1 wherein said aromatics solvent in step (d) is N-methylpyrrolidone.
Claim 6
Dependent Claim
25 words
The process of claim 1 wherein said obtained Bright Stock raffinate oil exhibits a Conradson Carbon Residue value of about 1.0 weight percent or less.
References Cited (Backward Citations)
US2146147A
Cited
US2079886A
Cited
US2163245A
Cited
US2570044A
Cited
US2889262A
Cited
US2939838A
Cited
US3074882A
Cited
US4168226A
Cited
US4419227A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1989-06-02 | 1989-12-02 | 1990-06-03 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1993-06-02 | 1993-12-02 | 1994-06-03 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1997-06-02 | 1997-12-02 | 1998-06-03 | $7700.00 | Window Closed / Lapsed |