US4391701A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for upgrading heavy oils
Assignee: IFP Energies nouvelles
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Filing: 1981-04-09
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Granted: 1983-07-05
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Expires: 2001-04-09
Abstract
Abstract The viscosity of heavy oils is reduced in order to facilitate pipe line transportation thereof. A fraction of the heavy oil is deasphalted in the presence of C 5 -C 7 hydrocarbons, a portion of the separated asphalt is converted to synthesis gas, at least a portion of said gas is used to manufacture an alcohol mixture including methanol and C 2 to C 10 alcohols, which mixture is admixed with the heavy oil before transportation thereof. This procedure is more beneficial to the transported heavy oil than the prior processes which do not comprise the conversion of the asphalt fraction of the heavy oil.
Inventors
- 👤 Jean-Francois Le Page
- 👤 Germain Martino
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-27 02:25
CPC Classifications
C; C10; C10L; C10L1/00; C10L1/10; C10L1/14; C10L1/18; C10L1/182; C10L1/1822; C10L1/1824; C07; C07C; C07C29/00; C07C29/15; C07C29/151; C07C29/1516; C07C29/1518; C07C29/48; C07C29/50; C10G; C10G57/00; Y; Y10; Y10S; Y10S208/00; Y10S208/95; Y10T; Y10T137/00; Y10T137/0318; Y10T137/0324; Y10T137/0329
Claims Analysis
Total Claims: 14
Claim 1
Independent Claim
102 words
A process for reducing the viscosity of a heavy oil, comprising the steps of: (a) deasphalting at least a portion of the heavy oil, and separately recovering a deasphalted heavy oil and asphaltenes; (b) gasifying at least a portion of said asphaltenes to produce a synthesis gas; (c) converting at least a portion of said synthesis gas to a mixture of alcohols consisting of methanol and at least one C 2-10 alcohol; and (d) admixing said alcohol mixture with the nondeasphalted heavy oil portion or with the deasphalted heavy oil or with a mixture thereof, to produce an oil of lower viscosity.
Claim 2
Dependent Claim
102 words
A process for reducing the viscosity of a heavy oil, comprising the steps of: (a) deasphalting at least a portion of the heavy oil, and separately recovering a deasphalted heavy oil and asphaltenes; (b) gasifying at least a portion of said asphaltenes to produce a synthesis gas; (c) converting at least a portion of said synthesis gas to a mixture of alcohols consisting of methanol and at least one C 2-10 alcohol; and (d) admixing said alcohol mixture with the nondeasphalted heavy oil portion or with the deasphalted heavy oil or with a mixture thereof, to produce an oil of lower viscosity.
Claim 3
Dependent Claim
33 words
A process according to claim 1, wherein the heavy oil is at least partly subjected to desalting, dehydration and separation of the solid sediments therefrom before deasphalting of at least a portion thereof.
Claim 4
Dependent Claim
28 words
A process according to claim 2 wherein the salt removal is performed by means of a fluxing agent consisting of at least a portion of the deasphalting solvent.
Claim 5
Dependent Claim
21 words
A process according to claim 2 wherein the deasphalting solvent consists essentially of a hydrocarbon having 5 carbon atoms per molecule.
Claim 6
Dependent Claim
20 words
A process according to claim 2, wherein the mixture of alcohols contains, by weight, about 60 to 85% of methanol.
Claim 7
Dependent Claim
20 words
A process according to claim 2, wherein the mixture of alcohols contains, by weight, from 10 to 50% of methanol.
Claim 8
Dependent Claim
19 words
A process according to claim 2, wherein the mixture of alcohols contains, by weight, 15 to 40% of methanol.
Claim 9
Dependent Claim
24 words
A process according to claim 1, wherein said oil of reduced viscosity contains, by weight, about 5 to 25% of said mixture of alcohols.
Claim 10
Dependent Claim
24 words
A process according to claim 1, wherein said heavy oil has a viscosity at 70° C. of close to or higher than 1000 centistokes.
Claim 11
Dependent Claim
69 words
A process according to claim 2, step (c) comprising feeding synthesis gas to a first zone for synthesizing: (i) methanol and at least one C 2-10 alcohol or (ii) substantially only at least one C 2-10 alcohol; and then feeding residual synthesis gas from said first zone to a second zone for methanol synthesis, and combining resultant alcohols from said first and second zones to form said alcohol mixture.
Claim 12
Dependent Claim
18 words
A process according to claim 9, wherein the resultant oil of lower viscosity is transported through a pipeline.
Claim 13
Dependent Claim
24 words
A process according to claim 1, wherein in step (c), the alcohols other than methanol produced from said synthesis gas are C 2-5 alcohols.
Claim 14
Dependent Claim
55 words
A process according to claim 2, wherein in step (d), said alcohol mixture is admixed with the deasphalted heavy oil; and wherein said process further comprises conveying the resultant oil of lower viscosity to a refinery; distilling the oil; and separating the fraction distilling below about 110° C. from the remainder of the heavy oil.
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) | 1986-07-04 | 1987-01-03 | 1987-07-05 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1990-07-04 | 1991-01-03 | 1991-07-05 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1994-07-04 | 1995-01-03 | 1995-07-05 | $7700.00 | Window Closed / Lapsed |