IP Library Granted Patent US 8,257,580
Granted Patent B2
US 8,257,580 · App. 12/512,758 · Granted Sep 4, 2012

Dry, stackable tailings and methods for producing the same

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Quick Facts
Patent No.
US 8,257,580
App. No.
12/512,758
Granted
Sep 4, 2012
Kind
B2
Abstract

Methods for preparing solvent-dry, stackable tailings. The methods may include a primary leaching or extraction process that separates most of the bitumen from a material comprising bitumen and produces first solvent-wet tailings. The first solvent-wet tailings are washed with a second solvent that removes the first solvent from the tailings. Second solvent remaining in the tailings is removed to thereby produce solvent-dry, stackable tailings.

Claims (73)

1. A method comprising:

forming a first mixture by mixing a material comprising bitumen with a first quantity of first solvent, wherein the first mixture comprises a bitumen-enriched solvent phase;

separating the bitumen-enriched solvent phase from the first mixture and thereby producing first solvent-wet tailings, wherein the first solvent-wet tailings comprise a first solvent component;

separating the first solvent component from the first solvent-wet tailings by adding a second solvent to the first solvent-wet tailings and thereby producing second solvent-wet tailings, wherein the second solvent-wet tailings comprise a second solvent component; and

separating the second solvent component from the second solvent-wet tailings and thereby forming solvent-dry, stackable tailings;

wherein the first solvent is a different type of solvent from the second solvent.

2. The method as recited in claim 1 , wherein separating the bitumen-enriched solvent phase from the first mixture comprises:

separating a first quantity of the bitumen-enriched solvent phase from the first mixture by filtering, settling or draining the bitumen-enriched solvent phase from the first mixture; and

separating a second quantity of the bitumen-enriched solvent phase from the first mixture by adding a second quantity of first solvent to the first mixture.

3. The method as recited in claim 2 , wherein separating the second quantity of the bitumen-enriched solvent phase from the first mixture comprises washing the first mixture with the second quantity of first solvent in a countercurrent process.

4. The method as recited in claim 1 , wherein separating the first solvent component from the first solvent-wet tailings comprises washing the first solvent-wet tailings with the second solvent in a countercurrent process.

5. The method as recited in claim 1 , wherein separating the second solvent from the second solvent-wet tailings comprises flashing the second solvent component from the second solvent-wet tailings.

6. The method as recited in claim 1 , wherein the first solvent comprises a light aromatic solvent.

7. The method as recited in claim 6 , wherein the light aromatic solvent comprises kerosene, diesel, gas oil, naphtha, benzene, toluene, an aromatic alcohol, derivatives thereof, or a combination thereof.

8. The method as recited in claim 1 , wherein the second solvent comprises a volatile hydrocarbon solvent.

9. The method as recited in claim 8 , wherein the volatile hydrocarbon solvent comprises a cyclo- or iso-paraffin having between 3 and 9 carbons derivatives thereof, or combinations thereof.

10. The method as recited in claim 1 , wherein the second solvent comprises liquefied petroleum gas.

11. The method as recited in claim 1 , wherein separating the bitumen-enriched solvent phase from the first mixture comprises filtering the first mixture in a plate and frame-type filter press.

12. The method as recited in claim 11 , wherein filtering the first mixture in a plate and frame-type filter press further comprises adding a gas over the first mixture loaded in the plate and frame-type filter press.

13. The method as recited in claim 1 , wherein separating the first solvent component from the first solvent-wet tailings comprises filtering the first solvent-wet tailings in a plate and frame-type filter press.

14. The method as recited in claim 13 , wherein filtering the first solvent-wet tailings in a plate and frame-type filter press further comprises adding a gas over the first solvent-wet tailings loaded in the plate and frame-type filter press.

15. The method as recited in claim 1 , wherein the material comprising bitumen comprises tar sands.

16. The method as recited in claim 1 , wherein the solvent-dry, stackable tailings comprise less than 0.1 wt % first solvent and second solvent.

17. Solvent-dry, stackable tailings produced by the method recited in claim 1 .

18. The method as claimed in claim 1 , further comprising:

upgrading a bitumen component of the bitumen-enriched solvent phase.

19. A method comprising:

forming a first mixture by mixing material comprising bitumen with a first quantity of first solvent;

loading the first mixture in a vertical column having a top end and bottom end;

injecting a second quantity of first solvent into the first mixture loaded in the vertical column at the top end of the vertical column;

collecting a bitumen-enriched solvent phase at the bottom end of the vertical column;

injecting a first quantity of second solvent into the first mixture loaded in the vertical column at the top end of the vertical column;

collecting a first solvent-enriched second solvent phase at the bottom end of the vertical column; and

discharging the first mixture from the vertical column;

wherein the first solvent is a different type of solvent from the second solvent.

20. The method as recited in claim 19 , further comprising adding a gas over the top end of the vertical column prior to injecting the second quantity of first solvent.

21. The method as recited in claim 19 , further comprising adding a gas over the top end of the vertical column after injecting the second quantity of first solvent and prior to injecting the first quantity of second solvent.

22. The method as recited in claim 19 , further comprising adding a gas over the top end of the vertical column after injecting the first quantity of second solvent.

23. The method as recited in claim 19 , wherein the first solvent comprises a light aromatic solvent.

24. The method as recited in claim 23 , wherein the light aromatic solvent comprises kerosene, diesel, gas oil, naphtha, benzene, toluene, an aromatic alcohol, derivatives thereof, or a combination thereof.

25. The method as recited in claim 19 , wherein the second solvent comprises a volatile hydrocarbon solvent.

26. The method as recited in claim 25 , wherein the volatile hydrocarbon solvent comprises a cyclo- or iso-paraffin having between 3 and 9 carbons, derivatives thereof, or combinations thereof.

27. The method as recited in claim 19 , wherein the second solvent comprises liquefied petroleum gas.

28. The method as recited in claim 19 , wherein the material comprising bitumen comprises tar sands.

29. The method as recited in claim 19 , further comprising separating a residual amount of second solvent from the first mixture prior to discharging the first mixture from the vertical column.

30. The method as recited in claim 29 , wherein separating a residual amount of second solvent from the first mixture comprises injecting a heated gas into the first mixture to evaporate the residual second solvent.

31. The method as recited in claim 19 , further comprising separating a residual amount of second solvent from the first mixture after discharging the first mixture from the vertical column.

32. The method as recited in claim 31 wherein separating a residual amount of second solvent from the first mixture comprises injecting a heated gas into the first mixture to evaporate the residual second solvent.

33. Solvent-dry, stackable tailings produced by the method recited in claim 19 .

34. The method as claimed in claim 19 , further comprising:

upgrading a bitumen component of the bitumen-enriched solvent phase.

35. A method comprising:

mixing a material comprising bitumen with a first quantity of first solvent;

separating a bitumen-enriched solvent phase from a first result of mixing the material comprising bitumen with the first quantity of first solvent mixture;

separating a first solvent component from a second result of separating the bitumen-enriched solvent phase from the first result; and

separating a second solvent component from a third result of separating the first solvent component from the second result;

wherein the first solvent is a different type of solvent from the second solvent.

36. The method as recited in claim 35 , wherein separating the bitumen-enriched solvent phase from the first result of mixing the material comprising bitumen with the first quantity of first solvent mixture comprises:

filtering, settling or draining a first quantity of bitumen-enriched solvent phase from the first result of mixing the material comprising bitumen with the first quantity of first solvent mixture; and

adding a second quantity of first solvent to the first result of mixing the material comprising bitumen with the first quantity of first solvent mixture.

37. The method as claimed in claim 35 , further comprising:

upgrading a bitumen component of the bitumen-enriched solvent phase.

38. A method comprising:

mixing material comprising bitumen with a first quantity of first solvent;

loading a first result of mixing material comprising bitumen with a first quantity of first solvent in a vertical column having a top end and bottom end;

injecting a second quantity of first solvent into the first result loaded in the vertical column at the top end of the vertical column;

collecting a bitumen-enriched solvent phase at the bottom end of the vertical column;

injecting a first quantity of second solvent into the first result loaded in the vertical column at the top end of the vertical column;

collecting a first solvent-enriched second solvent phase at the bottom end of the vertical column; and

discharging the first result from the vertical column;

wherein the first solvent is a different type of solvent from the second solvent.

39. The method as claimed in claim 38 , further comprising:

upgrading a bitumen component of the bitumen-enriched solvent phase.

Assignments (7)
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 Jul 2, 2014
From: MARATHON OIL CANADA CORPORATION
To: SHELL CANADA ENERGY; CHEVRON CANADA LIMITED
Reel/Frame 033233/0928 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 15, 2014
From: MARATHON OIL CANADA CORPORATION; ALBERTA CORPORATION
To: SHELL CANADA ENERGY; CHEVRON CANADA LIMITED
Reel/Frame 031971/0844 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 15, 2014
From: MARATHON OIL CANADA CORPORATION; ALBERTA CORPORATION
To: SHELL CANADA ENERGY; CHEVRON CANADA LIMITED
Reel/Frame 031971/0766 →
CHANGE OF NAME Recorded May 22, 2013
From: MARATHON CANADIAN OIL SANDS HOLDING LIMITED
To: MARATHON OIL CANADA CORPORATION
Reel/Frame 030467/0595 →
CHANGE OF NAME Recorded Jan 23, 2013
From: MARATHON OIL CANADA CORPORATION
To: MARATHON CANADIAN OIL SANDS HOLDING LIMITED
Reel/Frame 029676/0704 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 21, 2009
From: DUYVESTEYN, WILLEM P.C.; KIFT, JULIAN
To: MARATHON OIL CANADA CORPORATION
Reel/Frame 023128/0933 →