Geotechnical characteristics of tailings via lime addition
Methods and systems for treating tailings at an elevated pH using lime are disclosed herein. In some embodiments, the method comprises (i) providing a tailings stream comprising bicarbonates and a pH less than 9.0, (ii) adding a coagulant comprising calcium hydroxide to the tailings stream to form a mixture having a pH of at least 11.5 and a soluble calcium level no more than 800 mg/L, and (iii) dewatering the mixture to produce a product having a solids content of at least 40% by weight. In some embodiments, the pH and soluble calcium level of the mixture cause chemical modification of clay materials of the mixture via pozzolanic reactions. In some embodiments, the undrained shear strength of the product increases over a period of time of at least two days.
1. A method for treating a tailings stream, comprising:
providing a tailings stream comprising (i) a solids content of from 3% to 40% by weight, (ii) bicarbonates, and (iii) a pH less than 9.0;
adding a coagulant comprising calcium hydroxide to the tailings stream to form a mixture having a pH of at least 12.0 and a soluble calcium level of no more than 800 mg/L, wherein the pH and soluble calcium level promote pozzolanic reactions to occur within the mixture; and
after adding the coagulant to the tailings stream, dewatering the mixture to produce a product having a solids content of at least 40% by weight, wherein shear strength of the product increases over a period of time of at least two days to at least 1.5 kilopascals.
2. The method of claim 1 , wherein the shear strength of the product is an undrained shear strength that, after the period of time, is at least 5.0 kilopascals (kPa).
3. The method of claim 1 , wherein the period of time is at least 14 days.
4. The method of claim 1 , further comprising, prior to dewatering the mixture, adding a flocculant comprising a polymer to the mixture, wherein the polymer includes polyacrylamide.
5. The method of claim 1 , wherein dewatering comprises dewatering the mixture to produce release water, the method further comprising exposing the release water to air such that carbon dioxide of the air reacts with calcium of the release water to form at least one of calcium carbonate or a buffer comprising bicarbonates.
6. The method of claim 1 , wherein the mixture comprises clay provided via the tailings stream, and wherein the pH and the soluble calcium level of the mixture promotes pozzolanic reactions such that the clay is converted to calcium silicate hydrates and/or calcium aluminum hydrates.
7. The method of claim 1 , wherein the pozzolanic reactions occurring within the mixture do not produce gaseous carbon dioxide as a byproduct.
8. The method of claim 1 , wherein the calcium hydroxide comprises particles having a specific surface area of at least 25 m 2 /g.
9. The method of claim 1 , wherein the product, before the period of time, comprises particles having a d90 less than 20 microns, and wherein the d90 of the particle, after the period of time, is greater than 20 microns.
10. The method of claim 1 , wherein adding the coagulant comprises adding at least 8,000 ppm calcium hydroxide.
11. The method of claim 1 , wherein the shear strength is an undrained shear strength or undrained peak shear strength.
12. A method for treating tailings, comprising:
obtaining tailings comprising clay and bicarbonates;
combining at least a portion of the tailings with a first coagulant comprising calcium hydroxide to form a first mixture having a pH of at least 11.5 to no more than 12.0;
combining a second coagulant comprising calcium hydroxide with the first mixture to form a second mixture having a pH of at least 12.0 and a soluble calcium level of no more than 800 mg/L, wherein the pH and soluble calcium level promote pozzolanic reactions to occur within the second mixture; and
dewatering the second mixture to produce a product having a shear strength that increases over a period of time of at least two days to be at least 1.5 kilopascals.
13. The method of claim 12 , wherein combining at least a portion of the tailings with the first coagulant occurs in a first mixer upstream of a thickener vessel, and combining the second coagulant with the first mixture occurs within a second mixer downstream of the thickener vessel.
14. The method of claim 13 , further comprising separating, via the thickener vessel, the first mixture into release water and the second mixture.
15. The method of claim 12 , further comprising, prior to combining the second coagulant with the first mixture, removing or separating water from the first mixture.
16. The method of claim 12 , wherein the first mixture has a soluble calcium level of no more than 100 mg/L.
17. The method of claim 12 , further comprising adding a flocculant comprising a polymer to the first mixture, the polymer being configured to bond with clay of the first mixture.
18. A system for treating tailings, comprising:
a mixer or inline mixing area configured to
receive (i) tailings comprising clay and bicarbonates and (ii) a coagulant comprising calcium hydroxide, and
mix the tailings and coagulant to form a first mixture comprising a pH of at least 12.0 and a soluble calcium level of no more than 800 mg/L; and
a dewatering device configured to dewater the mixture to produce a product having a shear strength that increases over a period of time of at least two days to at least 1.5 kilopascals.
19. The system of claim 18 , wherein the shear strength of the product, after the period of time, is at least 5.0 kilopascals.
20. The system of claim 18 , wherein dewatering the mixture produces release water, the system further comprising a containment area configured to (i) receive the release water, and (ii) expose the release water to air such that carbon dioxide of the air reacts with alkaline calcium of the release water to form at least one of calcium carbonate or a buffer comprising bicarbonates or carbonates.
21. The system of claim 18 , wherein the coagulant is a slurry comprising 1% to 10% calcium hydroxide.
22. The system of claim 18 , wherein particles of the product, before the period of time, comprise a first average particle size, and wherein the particles, after the period of time, comprise a second average particle size larger than the first average particle size.