US4450067A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Distillation-induced extraction process
Assignee: Mobil Oil AS
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Filing: 1981-04-30
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Granted: 1984-05-22
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Expires: 2001-04-30
Abstract
Abstract A process for multi-solvent extraction is provided wherein polarity gradients induced by distillation are utilized for the extraction of petroleum residua and other heavy oils whereby a high quality maltenic fraction and a lower quality asphaltenic fraction are obtained.
Inventors
- 👤 Philip J. Angevine
- 👤 Michael B. Carroll
- 👤 Stuart S. Shih
- 👤 Samuel A. Tabak
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-09 01:48
CPC Classifications
C; C10; C10G; C10G21/00; C10G21/02
Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
137 words
An improved method of producing low CCR maltenic fractions and high CCR asphaltenic fractions from hydrocarbonaceous residua and other heavy oils by multisolvent-distillation-induced polarity gradient extraction comprising contacting two or more suitable solvents with said residua in a liquid flooded distillation column operating in a liquid continuous mode, said solvents having a high and a low boiling point with respect to one another, said higher boiling solvent having a higher relative polarity than said lower boiling solvent and each of said boiling points being sufficiently lower than that of the residua so that the solvents are distillted into high and low polarity fractions thereby forming a low CCR maltenic overhead stream and a high CCR asphaltenic bottoms stream and thereafter recovering the solvents from the overhead stream and the bottoms stream, and recycling the solvents for reuse.
Claim 2
Dependent Claim
137 words
An improved method of producing low CCR maltenic fractions and high CCR asphaltenic fractions from hydrocarbonaceous residua and other heavy oils by multisolvent-distillation-induced polarity gradient extraction comprising contacting two or more suitable solvents with said residua in a liquid flooded distillation column operating in a liquid continuous mode, said solvents having a high and a low boiling point with respect to one another, said higher boiling solvent having a higher relative polarity than said lower boiling solvent and each of said boiling points being sufficiently lower than that of the residua so that the solvents are distillted into high and low polarity fractions thereby forming a low CCR maltenic overhead stream and a high CCR asphaltenic bottoms stream and thereafter recovering the solvents from the overhead stream and the bottoms stream, and recycling the solvents for reuse.
Claim 3
Dependent Claim
65 words
The method of claim 1 wherein the solvents are selected from the group consisting of dimethyl formamide: 50/50 blend of dimethyl formamide and pentane; pentane; 50-50 blend of dimethyl formamide and heptane; heptane; glacial acetic acid, phenol, pyridine, toluene, mixtures of the above and suitable refinery streams admixed in at least a 50-50 ratio by weight of refinery stream to said solvents or solvent blends.
Claim 4
Dependent Claim
20 words
The method of claim 1 wherein the ratio of residua to solvent is about 1 to 20 at room temperature.
Claim 5
Dependent Claim
17 words
The method of claim 1 wherein the hydrocarbonaceous residua to be fractionated is a lubricating oil chargestock.
Claim 6
Dependent Claim
39 words
A process for preparing feedstock suitable for use in conventional refinery cracking processes wherein the hydrocarbonaceous residua is processed in accordance with the method of claim 1 and the low CCR stream is thereafter sent to a cracking unit.
Claim 7
Dependent Claim
46 words
A process for preparing feedstock suitable for use downstream in thermal processing units comprising treating petroleum residua or other heavy oils in accordance with the method of claim 1 and thereafter recovering and adapting the resultant high CCR stream for use in said thermal processing units.
Claim 8
Dependent Claim
48 words
A process for preparing feedstock suitable for use downstream in conventional refinery upgrading units comprising treating petroleum residua or other heavy oils in accordance with claim 1 and thereafter recovering both the high CCR stream and the low CCR stream for use in said suitable conventional upgrading units.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1987-05-22 | 1987-11-21 | 1988-05-22 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1991-05-22 | 1991-11-21 | 1992-05-22 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1995-05-22 | 1995-11-21 | 1996-05-22 | $7700.00 | Window Closed / Lapsed |