Non-aqueous extraction of bitumen from oil sands

Patent metadata

Field	Value
Publication number	US-11512256-B2
Application number	US-202016811929-A
Country	US
Kind code	B2
Filing date	Mar 6, 2020
Priority date	Sep 7, 2018
Publication date	Nov 29, 2022
Grant date	Nov 29, 2022

Abstract

A non-aqueous process for producing bitumen from oil sands is provided, and includes contacting oil sands and solvent to produce solvent diluted bitumen and solvent diluted tailings. The solvent diluted bitumen is subjected to a first fines separation stage that produces an overflow solvent diluted bitumen stream with residual fines that is subjected to a second fines separation stage to remove residual fines and produce a solvent diluted bitumen stream, which is subjected to solvent recovery. The fines streams are subjected to washing to produce washed tailings and solvent wash liquor comprising solvent and bitumen. Another non-aqueous process for producing bitumen from oil sands is provided, and includes subjecting oil sands to solvent extraction, including displacing the oil sands material and a solbit counter-currently and horizontally, and recovering a bitumen enriched solbit stream which is subjected to fines separation and subjecting the solvent diluted bitumen stream to solvent recovery.

First claim

The invention claimed is:

1. A non-aqueous process for producing bitumen from oil sands, comprising:
contacting oil sands and solvent in an extraction stage to produce a solvent diluted bitumen and a solvent diluted tailings comprising coarse mineral solids;
separating the solvent diluted bitumen from the solvent diluted tailings;
subjecting the solvent diluted bitumen to a fines separation stage to produce a fines enriched material that includes solvent, residual bitumen and fines and a solvent diluted bitumen stream with residual fines;
subjecting the solvent diluted bitumen stream to solvent recovery to produce recovered solvent and a bitumen product; and
subjecting the fines enriched material to a washing stage to remove residual bitumen and to produce a washed tailings and a solvent wash liquor comprising solvent and bitumen;
combining the solvent diluted tailings with a fluidizing stream comprising part of the solvent wash liquor from the washing stage.

2. The non-aqueous process of claim 1 , wherein the fines separation stage utilizes gravity separation.

3. The non-aqueous process of claim 1 , wherein the fines separation stage further comprises subjecting the solvent diluted tailings to an additional fines separation stage to remove at least a portion of the residual fines therefrom and produce the solvent diluted bitumen stream.

4. The non-aqueous process of claim 3 , wherein the additional fines separation stage utilizes enhanced solid-liquid separation.

5. The non-aqueous process of claim 3 , wherein the fines separation stage utilizes an inclined plate separator and a vertical centrifuge.

6. The non-aqueous process of claim 3 , wherein the fines separation stage is operated to effect bulk fines removal and the additional fines separation stage is operated to effect polishing to remove the at least a portion of the residual fines.

7. The non-aqueous process of claim 1 , wherein the fines separation is operated to produce the solvent diluted bitumen stream having below 5 wt % solids content.

8. The non-aqueous process of claim 1 , wherein the solvent diluted tailings and the fines enriched material are combined and supplied together to the washing stage to produce the washed tailings and the solvent wash liquor.

9. The non-aqueous process of claim 8 , wherein the washing stage comprises filtration.

10. The non-aqueous process of claim 9 , wherein the washing stage comprises overhead washing.

11. The non-aqueous process of claim 1 , wherein at least a portion of the solvent wash liquor is supplied back into the extraction stage.

12. The non-aqueous process of claim 1 , wherein the solvent diluted bitumen is pumped from the extraction stage to the fines separation stage.

13. The non-aqueous process of claim 1 , wherein the extraction stage is operated so as to perform the steps of:
displacing the oil sands and a solbit liquid comprising the solvent in counter-current and generally horizontal fashion with respect to each other, thereby forming a lower sand zone in contact with an upper solbit zone, the lower sand zone being subjected to mixing to extract bitumen from the oil sands material and cause extracted bitumen to dissolve into the solbit zone, wherein:
the lower sand zone comprises:
an upstream sand region having a high bitumen content; and
a downstream sand region having a lower bitumen content compared to the upstream sand region; and
the upper solbit zone comprises:
an upstream solbit region above the downstream region lower sand zone and having a low bitumen content; and
a downstream solbit region above the upstream region of the lower sand zone and having a high bitumen content; and
producing the solvent diluted bitumen from the downstream solbit region of the upper solbit zone.

14. The non-aqueous process of claim 13 , wherein the extraction stage is operated with counter-current flow of liquids and solids.

15. The non-aqueous process of claim 13 , wherein the solvent is preheated prior to being fed into the extraction stage.

16. The non-aqueous process of claim 15 , wherein the solvent supplied to the extraction stage is obtained in part from the solvent wash liquor.

17. A non-aqueous process for producing bitumen from oil sands, comprising:
subjecting oil sands to solvent extraction in an extraction stage to produce a solvent diluted bitumen and a solvent diluted tailings comprising coarse mineral solids, wherein the extraction stage comprises:
displacing an oil sands material and a solbit liquid in counter-current and generally horizontal fashion with respect to each other, thereby forming a lower sand zone in contact with an upper solbit zone, the lower sand zone being subjected to mixing to extract bitumen from the oil sands material and cause extracted bitumen to dissolve into the upper solbit zone, wherein:
the lower sand zone comprises:
an upstream sand region having a high bitumen content; and
a downstream sand region having a lower bitumen content compared to the upstream sand region; and
the upper solbit zone comprises:
an upstream solbit region above the downstream region of the lower sand zone and having a low bitumen content; and
a downstream solbit region above the upstream region of the lower sand zone and having a high bitumen content; and
recovering a bitumen enriched solbit stream as the solvent diluted bitumen from the downstream solbit region of the upper solbit zone;
subjecting the solvent diluted bitumen to fines separation to produce a fines enriched material that includes solvent, residual bitumen and fines and a solvent diluted bitumen stream depleted in fines;
supplying the fines enriched material to a washing stage to produce washed tailings and a solvent wash liquor;
adding a portion of the solvent wash liquor to the solvent diluted tailings to enable fluidization thereof downstream of the extraction stage; and
subjecting the solvent diluted bitumen stream to solvent recovery to produce a bitumen product and recovered solvent.

18. The non-aqueous process of claim 17 , wherein the extraction stage further comprises:
displacing a bitumen depleted sand from the downstream sand region of the lower sand zone vertically above the upper solbit zone to produce an elevated bitumen depleted sand; and
draining solvent and bitumen from the elevated bitumen depleted sand back into the upper solbit zone to thereby form the solvent diluted tailings.

19. The non-aqueous process of claim 18 , further comprising adding a solvent containing stream into the elevated bitumen depleted sand to wash bitumen therefrom.

20. The non-aqueous process of claim 18 , further comprising discharging the solvent diluted tailings as a solbit drained solid rich material.

21. The non-aqueous process of claim 17 , wherein the displacing and mixing is performed so that the lower sand zone is in slumped bed conditions.

22. The non-aqueous process of claim 17 , wherein the displacing and mixing is performed so that the lower sand zone is in expanded fluidized bed conditions.

23. The non-aqueous process of claim 17 , wherein subjecting the solvent diluted bitumen to fines separation comprises:
subjecting the solvent diluted bitumen to a first fines separation stage to produce a first bottoms stream that includes solvent, residual bitumen, the majority of fines and an overflow solvent diluted bitumen stream with residual fines; and
subjecting the overflow solvent diluted bitumen stream to a second fines separation

Assignees

• Suncor Energy Inc

Inventors

• Huq Iftikhar
• Abbaspour Ali
• Doucette Brian
• Hyndman Alexander
• Rideout Billy James

Classifications

• B03B9/02

  specially adapted for oil-sand, oil-chalk, oil-shales, ozokerite, bitumen, or the like · CPC title

• C10G1/045 Primary

  Separation of insoluble materials · CPC title

• B03B11/00

  Feed or discharge devices integral with washing or wet-separating equipment · CPC title

• C10G1/04 Primary

  by extraction · CPC title

• C10G2300/44

  Solvents · CPC title