Achieving water release zone for dewatering thick fine tailings based on shearing parameter such as camp number

Patent metadata

Field	Value
Publication number	US-11267730-B2
Application number	US-201916661855-A
Country	US
Kind code	B2
Filing date	Oct 23, 2019
Priority date	Jun 21, 2012
Publication date	Mar 8, 2022
Grant date	Mar 8, 2022

Abstract

Various techniques are provided in relation to flocculation and/or dewatering of thick fine tailings, with shear conditioning of flocculated tailings material in accordance with a pre-determined shearing parameter, such as the Camp Number. One example method of treating thick fine tailings including dispersing a flocculant into the thick fine tailings to form a flocculating mixture; shearing the flocculating mixture to increase yield stress and produce a flocculated mixture; shear conditioning the flocculated mixture to decrease the yield stress and break down flocs, the shear conditioning being performed in accordance with the pre-determined shearing parameter to produce conditioned flocculated material within a water release zone where release water separates from the conditioned flocculated material. The conditioned flocculated material can then be subjected to dewatering, for example by depositing, thickening or filtering. The design, construction and/or operation of a flocculation pipeline assembly can be facilitated.

First claim

The invention claimed is:

1. A method of dewatering thick fine tailings, comprising:
flocculating the thick fine tailings to produce a flocculated thick fine tailings material;
flowing the flocculated thick fine tailings material in a pipeline assembly under a laminar flow regime to shear condition the flocculated thick fine tailings material and break down flocs, the pipeline assembly having a pipe length and diameter sized substantially independent of flow rate of the flocculated thick fine tailings material and according to a pre-determined pipeline shearing parameter determined under laminar conditions and comprising residence time and shear rate, the pipeline assembly producing a conditioned flocculated material within a water release zone; and
dewatering the conditioned flocculated material while within the water release zone.

2. The method of claim 1 , wherein the flocculating step is performed in-line and comprises dispersing a flocculant into the thick fine tailings to form a flocculating mixture and shearing the flocculating mixture to build up flocs and produce the flocculated thick fine tailings material.

3. The method of claim 1 , wherein only a flocculant is added into the thick fine tailings prior to the dewatering.

4. The method of claim 1 , wherein the pre-determined shearing parameter is a pre-determined Camp Number.

5. The method of claim 4 , wherein the pre-determined shearing parameter is determined by mixing a flocculant with a sample thick fine tailings for producing a sample flocculating mixture under turbulent conditions to form a sample of the flocculated thick fine tailings material having a peak yield stress, and then shearing the sample of the flocculated thick fine tailings material under laminar conditions until the water release zone.

6. The method of claim 1 , wherein the dewatering comprises depositing the conditioned flocculated material onto a sub-aerial deposition area.

7. The method of claim 1 , wherein the dewatering comprises draining water away from solid flocculated material.

8. The method of claim 1 , wherein the dewatering comprises subjecting the conditioned flocculated material to thickening.

9. The method of claim 8 , wherein the thickening is performed in a thickener unit that produces a thickened underflow and an overflow.

10. The method of claim 1 , wherein the dewatering comprises subjecting the conditioned flocculated material to filtration.

11. The method of claim 1 , wherein the dewatering comprises supplying the conditioned flocculated material to a separation unit.

12. A method of dewatering thick fine tailings, comprising:
adding a flocculant into the thick fine tailings to produce a flocculation tailings material;
shear conditioning the flocculation tailings material in a pipeline assembly to produce a conditioned flocculated material within a water release zone wherein release water separates from the conditioned flocculated material;
providing sufficient mixing of the flocculant and the thick fine tailings prior to the shear conditioning, so as to enable the pipeline assembly to have a pipe length based on Camp Number scaling to achieve the water release zone; and
dewatering the conditioned flocculated material within the water release zone to produce a dewatered tailings material and release water.

13. The method of claim 12 , wherein the step of adding the flocculant is performed in-line and under turbulent flow conditions.

14. The method of claim 12 , wherein the step of providing sufficient mixing is performed in-line, and to increase a yield stress of the flocculation tailings material to a peak yield stress.

15. The method of claim 12 , wherein the step of providing sufficient mixing comprises subjecting the flocculation tailings material to turbulent flow conditions to build up flocs until reaching laminar flow conditions prior to the shear conditioning.

16. The method of claim 12 , wherein the Camp Number scaling comprises:
mixing a sample of the thick fine tailings with the flocculant under turbulent conditions to produce a sample flocculated mixture;
shearing the sample flocculated mixture under laminar conditions to determine a Camp Number for achieving the water release zone in the sample; and
providing the pipeline assembly with a length and a diameter for providing the flocculating tailings material with an amount of shear according to the Camp Number.

17. The method of claim 16 , wherein the mixing of the sample of the thick fine tailings with the flocculant and/or the shearing of the sample flocculated mixture is performed in a laboratory scale mixer.

18. The method of claim 12 , wherein the pipeline assembly comprises at least one in-line shear device having an equivalent pipe length.

Assignees

• Suncor Energy Inc

Inventors

• Weiss Marvin
• Sanchez Ana
• Bugg Trevor
• Revington Adrian

Classifications

• C10G1/045 Primary

  Separation of insoluble materials · CPC title

• C02F1/52 Primary

  by flocculation or precipitation of suspended impurities {(C02F1/463 takes precedence)} · CPC title

• C02F2103/10

  from quarries or from mining activities · CPC title

• C10G2300/208

  Sediments, e.g. bottom sediment and water or BSW · CPC title

• C10G2300/1033

  Oil well production fluids · CPC title