Claims
- 1. A method for removing solid fines in an extraction of bitumen from a carbonaceous solid or carbonaceous liquid containing extractable bitumen comprising:
- (a) forming a mixture comprising dissolved bitumen, about 5 to about 25 weight % undissolved bitumen, solid particle fines, and solvent wherein the about 5 to about 25 weight % undissolved bitumen is sufficient to settle from the mixture and remove the solid particle fines;
- (b) permitting the undissolved bitumen to settle with at least a portion of the solid fines agglomerating and settling with the undissolved bitumen to form a lower solid phase;
- (c) separating an upper dissolved bitumen solvent liquid phase from the lower solid phase; and
- (d) separating the dissolved bitumen from the solvent.
- 2. The method of claim 1 wherein about 7 to 15 weight % of the bitumen is undissolved.
- 3. The method of claim 1 wherein the amount of undissolved bitumen is sufficient to achieve a settling rate for the undissolved bitumen and agglomerated fines of at least 0.1 feet/hour.
- 4. A method for removing solid fines in an extraction of bitumen from a carbonaceous solid or carbonaceous liquid containing extractable bitumen comprising:
- (a) contacting the the carbonaceous solid or carbonaceous liquid containing extractable bitumen with a solvent mixture having a solubility parameter between about 8.5 and about 10.5 to produce a bitumen laden solvent mixture, wherein the solvent mixture comprises at least one solvent with a solubility parameter higher than that of bitumen and at least one solvent with a solubility parameter lower than that of bitumen;
- (b) separating sand from the bitumen laden solvent mixture;
- (c) treating the bitumen laden solvent mixture to remove the higher solubility parameter solvent so that an asphaltene fraction of the bitumen is precipitated from the remaining solvent to form a mixture comprising dissolved bitumen, undissolved asphaltenic bitumen, solid fines, and solvent;
- (d) permitting the undissolved asphaltenic bitumen to settle with at least a portion of the solid fines, agglomerating and settling with the undissolved asphaltenic bitumen;
- (e) separating the undissolved bitumen and solid fines; and
- (f) stripping the remaining solvent from the dissolved bitumen to produce product bitumen.
- 5. The method of claim 4 wherein the amount of undissolved asphaltenic bitumen is about 7 to about 15 weight percent.
- 6. The method of claim 4 wherein the higher solubility parameter solvent is selected from the group consisting of toluene, benzene, chlorobenzene, nitrobenzene, furan, dimethyl sulfide, carbon disulfide, triophene, pyridine, ketones of carbon number 5 or less, alcohols of carbon number 4 or less, chlorinated compounds of carbon number 2 or less, and mixtures thereof.
- 7. The method of claim 4 wherein the lower solubility parameter solvent is selected from the group consisting of cyclopentane, cyclohexane, naptha, kerosine, Freon-11, Freon-113, paraffins and olefins of carbon number 3 through 12, and mixtures thereof.
- 8. The method of claim 4 wherein the lower solubility parameter solvent is selected from the group consisting of paraffins of carbon number 8 to 12.
- 9. The method of claim 1 wherein the carbonaceous solid comprises tar sand, diatomaceous earth or a solid containing heavy oil.
- 10. The method of claim 1 wherein the solvent comprises at least one nonpolar hydrocarbon which is unsubstituted or substituted by at least one halogen, oxygen, nitrogen or sulfur atom and has from 1 to 15 carbon atoms.
BACKGROUND OF THE INVENTION
1. Reference to Related Application
This is a continuation-in-part application of copending application Ser. No. 449,607, "Recovery of a Carbonaceous Liquid with a Low Fines Content", L. B. Peck, and filed Dec. 14, 1982.
US Referenced Citations (8)
Non-Patent Literature Citations (2)
Entry |
Mitchell and Speight, Fuels, 52, 149 (1973). |
Fritschy and Papirer, Fuel, 57, 701 (1978). |
Continuation in Parts (1)
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Number |
Date |
Country |
Parent |
449607 |
Dec 1982 |
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