초록 ▼

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 sa

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.

대표청구항 ▼

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 sa

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; andadjusting 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; andadjusting 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 reagent into a flow of the tailings to cause dispersion of the flocculation reagent and build-up of flocs to form a flocculated tailings;(ii) transporting the flocculated tailings in-line and subjecting the flocculated tailings to shear conditioning to transform the flocculated tailings into a gel stage flocculated tailings;(iii) subjecting the gel stage flocculated tailings to shear conditioning to form an ungelled flocculated tailings material within a floc breakdown and water release while avoiding overshearing the ungelled flocculated tailings material, the ungelled flocculated tailings having a decreased yield shear stress;(iv) subjecting the ungelled flocculated tailings material to dewatering;wherein the 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%. 27. The process of claim 26, wherein stages (i), (ii) and (iii) are performed in a pipeline reactor. 28. The process of claim 27, wherein the pipeline reactor comprises a co-annular injection device for in-line injection of the flocculant solution within the tailings. 29. The process of claim 26, wherein the flocculant solution is in the form of an aqueous solution in which the flocculation reagent is substantially dissolved. 30. The process of claim 29, wherein the flocculation reagent comprises a polymer flocculant that is shear-responsive in stage (i) thereby dispersing throughout the tailings, and enables shear-resilience during stages (ii) and (iii). 31. The process of claim 30, wherein the flocculation reagent comprises a polymer flocculant that is selected according to a screening method comprising: preparing a sample flocculation matrix comprising a sample of the 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 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. 32. The process of claim 31, wherein the water release response is determined by measuring capillary suction time (CST) of the sample flocculation matrix. 33. The process of claim 32, further comprising: measuring the capillary suction time (CST) of the flocculated tailings during stages (ii) and (iii) to obtain a minimum CST interval on a curve of CST versus time; andadjusting the shear conditioning imparted to the flocculated tailings so as to ensure dewatering of the flocculated tailings material within the minimum CST interval. 34. The process of claim 26, further comprising: measuring the yield shear stress of the flocculated tailings during stages (ii) and (iii);identifying a decrease zone following a plateau zone; andadjusting the shear conditioning in stages (ii) and (iii) to ensure dewatering of the ungelled flocculated tailings material within the decrease zone. 35. The process of claim 34, wherein the shear conditioning is managed by adjusting the length of pipeline through which the flocculated tailings travels prior to dewatering. 36. The process of claim 34, wherein stage (iv) of subjecting the ungelled flocculated 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. 37. The process of claim 26, wherein subjecting the ungelled flocculated tailings material to dewatering comprises expelling the ungelled flocculated tailings material from a conditioning pipeline. 38. The process of claim 26, wherein subjecting the ungelled flocculated tailings material to dewatering comprises supplying the ungelled flocculated tailings material to a dewatering device. 39. The process of claim 38, wherein the dewatering device comprises a filter, a thickener, a centrifuge, or a cyclone. 40. The process of claim 37, wherein expelling the ungelled flocculated tailings material from the conditioning pipeline comprises depositing the ungelled flocculated tailings material onto a solid land surface to form a deposit and to allow the released water to flow away from the deposit. 41. The process of claim 40, wherein the ungelled flocculated tailings material is deposited into a deposition cell having a sloped bottom surface that is sloped between about 1% and about 7%. 42. The process of claim 41, 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 tailings material. 43. The process of claim 42, further comprising providing furrows in the deposit, the furrows providing water flow paths. 44. The process of claim 43, wherein substantially all of the furrows extend lengthwise in the same general direction as the sloped bottom surface. 45. The process of claim 40, wherein the solid land surface comprises a multi-cell configuration of deposition cells. 46. The process of claim 45, 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 tailings by varying the pipeline length to a corresponding deposition cell. 47. The process of claim 45, wherein at least some of the deposition cells are arranged in toe-to-toe relationship to share a common water drainage ditch. 48. The process of claim 26, further comprising imparting sufficient hydraulic pressure to the tailings upstream of stage (i) such that downstream pumping is not required. 49. The process of claim 26, 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. 50. The process of claim 40, 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. 51. The process of claim 26, wherein the tailings comprise fine tailings. 52. The process of claim 26, wherein the tailings comprise oil sands fine tailings. 53. The process of claim 52, wherein the oil sands fine tailings are oil sands mature fine tailings. 54. The process of claim 26, wherein the tailings comprise colloidal fluids having non-Newtonian fluid behavior. 55. A process for dewatering a colloidal fluid having non-Newtonian fluid behavior, comprising: (i) adding a flocculant solution comprising an effective amount of flocculation reagent into a flow of the colloidal fluid to cause dispersion of the flocculation reagent and build-up of flocs to form a flocculated colloidal fluid;(ii) transporting the flocculated colloidal fluid in-line and subjecting the flocculated colloidal fluid to shear conditioning to transform the flocculated colloidal fluid into a gel stage flocculated colloidal fluid;(iii) subjecting the gel stage flocculated colloidal fluid to shear conditioning to form an ungelled flocculated colloidal fluid material within a floc breakdown and water release stage while avoiding overshearing the ungelled flocculated colloidal fluid material, the ungelled flocculated colloidal fluid material having a decreased yield shear stress;(iv) subjecting the ungelled flocculated colloidal fluid material to dewatering;wherein the colloidal fluid 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%.