Patent US4681872A successfully refreshed from Google Patents.
Patent DE322983C successfully refreshed from Google Patents.
Patent US4634520A successfully refreshed from Google Patents.
US4634520A
Expired / Lapsed
US
⏱️ 0.0 years remaining
De-asphalting heavy crude oil and heavy crude oil/water emulsions
Assignee: BITECH Corp
•
Filing: 1984-10-22
•
Granted: 1987-01-06
•
Expires: 2004-10-22
Abstract
Abstract A process for the simultaneous de-emulsification and de-asphalting of heavy oil/water emulsions containing asphaltics enables de-asphalted oil, asphaltics and emulsion water to be separately recovered. A heavy oil/water emulsion is mixed with a solvent to cause the emulsion to be broken with consequent dissolution of oil by the solvent and coalescence of emulsion water and asphaltics as fast settling particles, the solvent comprising a light C 4 to C 7 paraffinic composition and the weight of solvent being from about 2 to about 5 times the weight of heavy oil. The water/asphaltic particles are separated from the bulk of the oil/solvent phase and are fed into a water bath to produce relatively large stable asphaltic agglomerates with exclusion of emulsion water. The asphaltic agglomerates are removed from the hot water bath, and de-asphalted oil is recovered from the oil/solvent phase. Heavy oil containing asphaltics can also be treated by the process, with the separated asphaltics agglomerating in the hot water bath.
Inventors
- 👤 Georgi Angelov
- 👤 Paul W. M. Shibley
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-09 06:31
CPC Classifications
C; C10; C10G; C10G33/00; C10G33/04; C10G21/00; C10G21/003
Claims Analysis
Total Claims: 11
Claim 1
Independent Claim
178 words
A process for the simultaneous de-emulsification and de-asphalting of heavy oil/water well head emulsions containing asphaltics which enables de-asphalted oil, asphaltics and emulsion water to be separately recovered, said process comprising: mixing a heavy oil/water well head emulsion with a solvent to cause the emulsion to be broken with consequent dissolution of oil by the solvent and coalescence of emulsion water and asphaltics as fast settling particles, said solvent comprising a light C 4 to C 7 paraffinic composition and the weight of solvent being from about 2 to about 5 times the weight of heavy oil, said fast settling particles each comprising a water droplet stabilized by a sheath of asphaltics, separating the water/asphaltic particles from the bulk of the oil/solvent phase, feeding the separated water/asphaltic particles and residual solvent into a hot water bath to produce relatively large stable asphaltic agglomerates with exclusion of emulsion water and with said residual solvent being flashed off, recovering the flashed off solvent, removing the asphaltic agglomerates from the hot water bath, and recovering de-asphalted oil from the oil/solvent phase.
Claim 2
Dependent Claim
178 words
A process for the simultaneous de-emulsification and de-asphalting of heavy oil/water well head emulsions containing asphaltics which enables de-asphalted oil, asphaltics and emulsion water to be separately recovered, said process comprising: mixing a heavy oil/water well head emulsion with a solvent to cause the emulsion to be broken with consequent dissolution of oil by the solvent and coalescence of emulsion water and asphaltics as fast settling particles, said solvent comprising a light C 4 to C 7 paraffinic composition and the weight of solvent being from about 2 to about 5 times the weight of heavy oil, said fast settling particles each comprising a water droplet stabilized by a sheath of asphaltics, separating the water/asphaltic particles from the bulk of the oil/solvent phase, feeding the separated water/asphaltic particles and residual solvent into a hot water bath to produce relatively large stable asphaltic agglomerates with exclusion of emulsion water and with said residual solvent being flashed off, recovering the flashed off solvent, removing the asphaltic agglomerates from the hot water bath, and recovering de-asphalted oil from the oil/solvent phase.
Claim 3
Dependent Claim
58 words
A process according to claim 1 wherein the heavy water/oil emulsion and solvent mixture is at an elevated temperature less than about 110° C. while maintaining the solvent in liquid form to cause the emulsion to be broken with consequent dissolution of heavy oil by the solvent and coalescence of emulsion water and asphaltics as fast settling particles.
Claim 4
Dependent Claim
27 words
A process according to claim 1 wherein the separated water/asphaltic particles are washed with fresh solvent to remove residual oil before feeding into the hot water bath.
Claim 5
Dependent Claim
23 words
A process according to claim 1 wherein the solvent is selected from the group consisting of butane, pentane, petrolether, hexane and mixtures thereof.
Claim 6
Dependent Claim
25 words
A process according to claim 1 wherein the temperature of the hot water bath is between the boiling temperature of the solvent and 100° C.
Claim 7
Dependent Claim
27 words
A process according to claim 1 wherein sand and/or clay is associated with the heavy oil and is agglomerated in the hot water bath with the asphaltics.
Claim 8
Dependent Claim
18 words
A process according to claim 6 wherein sand and/or clay cause the agglomerates to sink in the bath.
Claim 9
Dependent Claim
13 words
A process according to claim 1 wherein the agglomerates float in the bath.
Claim 10
Dependent Claim
24 words
A process according to claim 1 wherein acid or alkali is added to the hot water bath to facilitate production of the asphaltic agglomerates.
Claim 11
Dependent Claim
25 words
A process according to claim 1 wherein metal values in the emulsion water are precipitated in the hot water bath and agglomerated with the asphaltics.
References Cited (Backward Citations)
GB134088A
Cited
US1472384A
Cited
US2235639A
Cited
US2383362A
Cited
US3321394A
Cited
US3434967A
Cited
US3696021A
Cited
GB1340022A
Cited
US3733259A
Cited
US3779895A
Cited
GB1384290A
Cited
US4021335A
Cited
US4125458A
Cited
GB2024849A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1990-01-05 | 1990-07-07 | 1991-01-06 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1994-01-05 | 1994-07-07 | 1995-01-06 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1998-01-05 | 1998-07-07 | 1999-01-06 | $7700.00 | Window Closed / Lapsed |