Process for flocculating and dewatering oil sand mature fine tailings

Patent metadata

Field	Value
Publication number	US-9909070-B2
Application number	US-201013496176-A
Country	US
Kind code	B2
Filing date	Apr 22, 2010
Priority date	Sep 15, 2009
Publication date	Mar 6, 2018
Grant date	Mar 6, 2018

Abstract

A process for dewatering oil sand fine tailings is provided and comprises a dispersion and floc build-up stage comprising in-line addition of a flocculent solution comprising an effective amount of flocculation reagent into a flow of the oil sand fine tailings; a gel stage wherein flocculated oil sand fine tailings is transported in-line and subjected to shear conditioning; a floc breakdown and water release stage wherein the flocculated oil sand fine tailings releases water and decreases in yield shear stress, while avoiding an oversheared zone; depositing the flocculated oil sand fine tailings onto a deposition area to form a deposit and to enable the release water to flow away from the deposit, preferably done in a pipeline reactor and managing shear according to yield stress and CST information and achieves enhanced dewatering.

First claim

The invention claimed is:

1. A process for dewatering oil sand fine tailings, comprising:
(i) adding a flocculant solution comprising an effective amount of flocculation reagent in-line into a flow of the oil sand fine tailings to cause dispersion of the flocculation reagent and build-up of flocs to form a flocculated oil sand fine tailings;
(ii) transporting the flocculated oil sand fine tailings in-line and subjecting the flocculated oil sand fine tailings to shear conditioning to transform the flocculated oil sand fine tailings into a gel stage flocculated oil sand fine tailings;
(iii) subjecting the gel stage flocculated oil sand fine tailings to shear conditioning to form an ungelled flocculated oil sand fine tailings material within a floc breakdown and water release stage while avoiding overshearing the ungelled flocculated oil sand fine tailings material, the ungelled flocculated oil sand fine tailings material having a decreased yield shear stress;
(iv) subjecting the ungelled flocculated oil sand fine tailings material to dewatering;
wherein the oil sand fine tailings comprise solids in a concentration of between about 15 wt % and about 45 wt %, the solids having a clay content of at least about 45%.

2. The process of claim 1 , wherein stages (i), (ii) and (iii) are performed in a pipeline reactor.

3. The process of claim 2 , wherein the pipeline reactor comprises a co-annular injection device for in-line injection of the flocculant solution within the oil sand fine tailings.

4. The process of claim 3 , wherein the flocculant solution is in the form of an aqueous solution in which the flocculation reagent is substantially dissolved.

5. The process of claim 4 , wherein the flocculation reagent comprises a polymer flocculant that is shear-responsive in stage (i) thereby dispersing throughout the oil sand fine tailings, and enables shear-resilience during stages (ii) and (iii).

6. The process of claim 5 , wherein the polymer flocculant that is selected according to a screening method comprising:
preparing a sample flocculation matrix comprising a sample of the oil sand fine tailings and a sample polymer flocculant;
imparting a first shear conditioning to the sample flocculation matrix for rapidly mixing the polymer flocculant with the sample of the oil sand fine tailings, followed by imparting a second shear conditioning to the sample flocculation matrix that is substantially lower than the first shear conditioning;
determining a water release response after both the first and second shear conditionings have been imparted;
wherein when the water release response is increased compared to a single water release response obtained when either one of the first or second shear conditioning is imparted as a single shear conditioning step, the polymer flocculant is selected for the process.

7. The process of claim 6 , wherein the water release response is determined by measuring capillary suction time (CST) of the sample flocculation matrix.

8. The process of claim 7 , further comprising:
measuring the capillary suction time (CST) of the flocculated oil sand fine tailings during stages (ii) and (iii) to obtain a minimum CST interval on a curve of CST versus time; and
adjusting the shear conditioning imparted to the flocculated oil sand fine tailings so as to ensure dewatering of the ungelled flocculated oil sand fine tailings material within the minimum CST interval.

9. The process of claim 2 , further comprising:
measuring the yield shear stress of the flocculated oil sand fine tailings during stages (ii) and (iii);
identifying a decrease zone following a plateau zone; and
adjusting the shear conditioning in stages (ii) and (iii) to ensure dewatering of the ungelled flocculated oil sand fine tailings material within the decrease zone.

10. The process of claim 9 , wherein the shear conditioning is managed by adjusting the length of pipeline through which the flocculated oil sand fine tailings travels prior to dewatering.

11. The process of claim 9 , wherein stage (iv) of subjecting the ungelled flocculated oil sand fine tailings material to dewatering is performed within the decrease zone of the yield shear stress and within a minimum capillary suction time (CST) interval, the minimum CST interval being obtained on a curve of CST versus time.

12. The process of claim 1 , wherein subjecting the ungelled flocculated oil sand fine tailings material to dewatering comprises expelling the ungelled flocculated oil sand fine tailings material from a conditioning pipeline.

13. The process of claim 1 , wherein subjecting the ungelled flocculated oil sand fine tailings material to dewatering comprises supplying the ungelled flocculated oil sand fine tailings material to a dewatering device.

14. The process of claim 13 , wherein the dewatering device comprises a filter, a thickener, a centrifuge, or a cyclone.

15. The process of claim 12 , wherein expelling the ungelled flocculated oil sand fine tailings material from the conditioning pipeline comprises depositing the ungelled flocculated oil sand fine tailings material onto a solid land surface to form a deposit and to allow the released water to flow away from the deposit.

16. The process of claim 15 , wherein the ungelled flocculated oil sand fine tailings material is deposited into a deposition cell having a sloped bottom surface that is sloped between about 1% and about 7%.

17. The process of claim 16 , further comprising mechanically working the deposit to spread the deposit over the deposition cell and impart additional shear thereto while avoiding overshearing the ungelled flocculated oil sand fine tailings material.

18. The process of claim 17 , further comprising providing furrows in the deposit, the furrows providing water flow paths.

19. The process of claim 18 , wherein substantially all of the furrows extend lengthwise in the same general direction as the sloped bottom surface.

20. The process of claim 15 , wherein the solid land surface comprises a multi-cell configuration of deposition cells.

21. The process of claim 20 , wherein the deposition cells of the multi-cell configuration are provided at different distances from the in-line addition of the flocculant solution to allow varying the shear conditioning imparted to the flocculated oil sand fine tailings by varying the pipeline length to a corresponding deposition cell.

22. The process of claim 20 , wherein at least some of the deposition cells are arranged in toe-to-toe relationship to share a common water drainage ditch.

23. The process of claim 15 , wherein the deposit dewaters due to drainage of release water and evaporative drying, the drainage accounting for at least about 60 wt % of water loss, and drainage occurring at a rate of at least about 1.4 wt % solids increase per day until the deposit reaches about 55 wt % to 60 wt % solids.

24. The process of claim 1 , further comprising imparting sufficient hydraulic pressure to the oil sand fine tailings upstream of stage (i) such that downstream pumping is not required.

25. The process of claim 1 , wherein the stage (i) dispersion is further characterized in that second moment M is between about 1.0 and about 2.0 at a downstream location about 5 pipe diameters from adding the flocculant solution.

26. A process for dewatering tailings, comprising:
(i) adding a flocculant solution comprising an effective amount of flocculation re

Assignees

• Revington Adrian Peter
• Omotoso Oladipo
• Wells Patrick Sean
• Hann Thomas Charles
• Weiss Marvin Harvey
• Bugg Trevor
• Eastwood Jamie
• Young Stephen Joseph
• Oneill Hugues Robert
• Sanchez Ana Cristina
• Suncor Energy Inc

Inventors

• Revington Adrian Peter
• Omotoso Oladipo
• Wells Patrick Sean
• Hann Thomas Charles
• Weiss Marvin Harvey
• Bugg Trevor
• Eastwood Jamie
• Young Stephen Joseph
• Oneill Hugues Robert
• Sanchez Ana Cristina

Classifications

• C02F1/56

  Macromolecular compounds · CPC title

• C10G33/04

  with chemical means · CPC title

• C02F2103/10

  from quarries or from mining activities · CPC title

• C10G1/047 Primary

  Hot water or cold water extraction processes · CPC title

• B01F2005/0034

  Operations & Transport · mapped topic