Mineral ore flotation using carboxymethyl cellulose with different characteristics in different flotation cells
A flotation method for mineral processing is disclosed. The method for floating includes a first step of using a first carboxymethyl cellulose (CMC) in a first flotation cell, and a subsequent step includes using a second CMC in a subsequent flotation cell, the first and second CMCs having different characteristics. The first flotation cell may be used in at least one rougher stage and/or at least one rougher-scavenger stage of the flotation method, and the subsequent flotation cell may be used in at least one cleaner stage, and/or at least one cleaner scavenger stage, and/or at least one recleaner stage of the flotation method. A product may be obtained, directly or indirectly, by such a method. A mineral processing plant may use at least two CMCs of different characteristics in flotation for mineral processing.
1. A method for floating, the method comprising:
a first step comprising using a first carboxymethyl cellulose (CMC) in a first flotation cell to produce a first concentrate from a feed, and
feeding, directly or indirectly, the first concentrate to a subsequent step comprising using a second CMC in a subsequent flotation cell to produce a product,
wherein the first and second CMCs have one or more different characteristics.
2. The method of claim 1 , wherein the first CMC has a degree of substitution (DS) that is different from a DS of the second CMC.
3. The method of claim 2 , wherein the DS of the first CMC is lower than the DS of the second CMC.
4. The method of claim 1 , wherein the first flotation cell is comprised in at least one rougher stage and/or at least one rougher-scavenger stage of the flotation method, and the subsequent flotation cell is comprised in at least one cleaner stage, and/or at least one cleaner scavenger stage, and/or at least one recleaner stage of the flotation method.
5. The method of claim 2 , wherein the difference in DS is at least 0.4.
6. The method of claim 2 , wherein the DS of the first CMC is in the range of 0.4-0.9 and the DS of the second CMC is in the range of 0.8-1.5.
7. The method of claim 2 , wherein the DS of the first CMC is about 0.44 or 0.53 and the DS of the second CMC is about 1.1.
8. The method of claim 1 , wherein the first CMC has a viscosity that is different from a viscosity of the second CMC.
9. The method of claim 1 , wherein the first CMC has a molecular weight that is different from a molecular weight of the second CMC.
10. The method of claim 1 , wherein the product is a concentrate of minerals.
11. The method of claim 1 , wherein the product is a base metal sulphide concentrate.
12. The method of claim 1 , wherein the product is a base metal Cu—Ni sulphide concentrate.