IP Library Granted Patent US 8,728,306
Granted Patent B2
US 8,728,306 · App. 13/424,538 · Granted May 20, 2014

Method for extracting bitumen from an oil sand feed stream

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Quick Facts
Patent No.
US 8,728,306
App. No.
13/424,538
Granted
May 20, 2014
Kind
B2
Abstract

A method for extracting bitumen from an oil sand feed stream comprises at least the steps of: (a) providing an oil sand feed stream; (b) contacting the oil sand feed stream with a liquid comprising an aliphatic hydrocarbon solvent thereby obtaining a solvent-diluted oil sand slurry; (c) filtering the solvent-diluted oil sand slurry, thereby obtaining a first bitumen-enriched filtrate, a second bitumen-depleted filtrate and a bitumen-depleted sand; (d) reusing the second filtrate obtained in step (c) in the contacting of step (b); and (e) removing solvent from the first bitumen-enriched filtrate thereby obtaining a bitumen-enriched stream.

Claims (17)

1. A method for extracting bitumen from an oil sand feed stream, the method comprising at least the steps of:

(a) providing an oil sand feed stream;

(b) contacting the oil sand feed stream with a liquid comprising an aliphatic hydrocarbon solvent thereby obtaining a solvent-diluted oil sand slurry;

(c) filtering the solvent-diluted oil sand slurry, thereby obtaining a first bitumen-enriched filtrate, a second bitumen-depleted filtrate and a bitumen-depleted sand;

(d) reusing the second filtrate obtained in step (c) in the contacting of step (b); and

(e) removing solvent from the first bitumen-enriched filtrate thereby obtaining a bitumen-enriched stream.

2. The method according to claim 1 , wherein the solvent in step (b) comprises an aliphatic hydrocarbon having from 3 to 9 carbon atoms per molecule.

3. The method according to claim 1 , wherein the solvent in step (b) comprises a saturated hydrocarbon.

4. The method according to claim 1 , wherein the particles of the solvent-diluted oil sand slurry obtained in step (b) are screened or reduced in size to have a diameter below 5.0 cm.

5. The method according to claim 1 wherein the solvent-diluted oil sand slurry obtained in step (b) has a solvent-to-bitumen (S/B) weight ratio of from 1.2 to 4.0.

6. The method according to claim 1 wherein the solvent-diluted oil sand slurry obtained in step (b) comprises from 32 to 60 vol. % of solids.

7. The method according to claim 1 wherein the first filtrate obtained in step (c) has a S/B weight ratio of from 1.0 to 5.0.

8. The method according to claim 1 wherein the second filtrate obtained in step (c) has a SB weight ratio of above 3.0.

9. The method according to claim 1 wherein the solvent removed from the first filtrate in step (e) is reused in step (c).

10. The method according to claim 9 , wherein at least part of the solvent removed from the first filtrate is removed as vapour.

11. The method according to claim 10 , wherein at least part of the vapour is condensed in step (c).

12. The method according to claim 1 wherein the bitumen-depleted sand stream is dried, thereby obtaining a dried bitumen-depleted sand stream containing less than 500 ppmw.

Assignments (2)
NUNC PRO TUNC ASSIGNMENT Recorded Feb 27, 2018
From: SHELL CANADA ENERGY
To: CANADIAN NATURAL UPGRADING LIMITED
Reel/Frame 045054/0463 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 15, 2012
From: PLOEMEN, INGMAR HUBERTUS JOSEPHINA; SCHOONEBEEK, RONALD JAN; IN'T VEEN, BERNARDUS CORNELIS MARIA
To: SHELL OIL COMPANY
Reel/Frame 028211/0165 →