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US4592832A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for increasing Bright Stock raffinate oil production

Assignee: ExxonMobil Technology and Engineering Co
•
Filing: 1984-09-06
•
Granted: 1986-06-03
•
Expires: 2004-09-06
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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 20:11
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)

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US2079886A Cited
US2163245A Cited
US2570044A Cited
US2889262A Cited
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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

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