Flotation of fine-grained materials

Claim 2

A process for treating a fine mineral consisting substantially completely of particles smaller than 50 microns equivalent spherical diameter in order to separate therefrom mineral impurities, which process comprises the steps of (a) conditioning the fine mineral in the form of an aqueous slurry, having a solids content of at least 30 percent by weight and containing a deflocculant, for a time sufficient to dissipate therein at least 25 horsepower hours of energy per ton of mineral solids; (b) mixing with the aqueous mineral slurry before or during the conditioning thereof a collector; (c) introducing the conditioned mineral slurry into a froth flotation cell having a central, internal, submerged impeller which comprises a base plate, to which there are attached a plurality of blades in radial arrangement, and a stationary cover plate separated from the tips of the blades by a small clearance; and (d) thereafter subjecting the conditioned aqueous mineral slurry to a pumping action in a froth flotation process in which the impeller of said froth flotation cell has a peripheral speed of at least 2,000 feet/minute and in which the aeration rate is at least 0.8 cubic feet of air per minute per cubic foot of froth flotation cell volume.

Claim 3

A process according to claim 1, wherein said impeller has a peripheral speed of at least 2,500 feet/minute.

Claim 4

A process according to claim 1, wherein the impeller has a diameter which is at least three times its axial height.

Claim 5

A process according to claim 1, wherein the fine mineral is conditioned as an aqueous slurry having a solids content in the range 40 percent to 60 percent by weight.

Claim 6

A process according to claim 1, wherein the fine mineral is a kaolinitic clay.

Claim 7

A process according to claim 1, wherein the conditioned mineral slurry is introduced into the froth flotation cell at a solids content in the range 15 percent to 30 percent by weight.

Claim 8

A process according to claim 1 for treating a fine mineral consisting substantially completely of particles smaller than 50 microns equivalent spherical diameter in order to separate therefrom mineral impurities, which process comprises the steps of (a) conditioning the fine mineral in the form of an aqueous slurry, having a solids content of at least 30 percent by weight and containing a deflocculant, for a time sufficient to dissipate therein at least 25 horsepower hours of energy per ton of mineral solids; (b) mixing with the aqueous mineral slurry before or during the conditioning thereof a collector; (c) diluting the conditioned mineral slurry to a solids content in the range 15 to 30 percent by weight; (d) introducing the diluted, conditioned mineral slurry into a froth flotation cell having a central, internal, submerged impeller which comprises a base plate, to which are attached a plurality of blades in radial arrangement, and a stationary cover plate separated from the tips of the blades by a small clearance; and (e) thereafter subjecting the conditioned aqueous mineral slurry to a pumping action in a froth flotation process in which the impeller of said froth flotation cell has a peripheral speed of at least 2,500 feet/minute and in which the aeration rate is at least 0.8 cubic feet of air per minute per cubic foot of froth flotation cell volume.

Claim 9

A process according to claim 7, wherein the impeller has a diameter which is at least three times its axial height.

Claim 10

A process according to claim 7, wherein the fine mineral is conditioned as an aqueous slurry having a solids content in the range 40 to 60 percent by weight.

Claim 11

A process according to claim 1 for treating a fine mineral consisting substantially completely of particles smaller than 50 microns equivalent spherical diameter in order to separate therefrom mineral impurities, which process comprises the steps of (a) conditioning the fine mineral in the form of an aqueous slurry containing a deflocculant, the aqueous slurry having a solids content in the range 40 to 60 percent by weight, for a time sufficient to dissipate therein at least 25 horsepower hours of energy per ton of mineral solids; (b) mixing with the aqueous mineral slurry before or during the conditioning thereof a collector; (c) diluting the conditioned mineral slurry to a solids content in the range 15 to 30 percent by weight; (d) introducing the diluted, conditioned mineral slurry into a froth flotation cell having a central, internal, submerged impeller which comprises a base plate, to which there are attached a plurality of blades in radial arrangement, and a stationary cover plate separated from the tips of the blades by a small clearance, the impeller having a diameter which is at least three times its axial height; and (e) subjecting the conditioned aqueous mineral slurry to a pumping action in a froth flotation process in which the impeller of said froth flotation cell has a peripheral speed of at least 2,500 feet/minute and in which the aeration rate is at least 0.8 cubic feet of air per minute per cubic foot of froth flotation cell volume.

Claim 12

A process according to claim 10, wherein said fine mineral is a kaolinitic clay.

Claim 13

A process according to claim 10, wherein said fine mineral is a celestite ore.

Claim 14

A process according to claim 10, wherein said fine mineral is an apatite ore.

Claim 15

A process according to claim 1 for treating a fine mineral consisting substantially completely of particles smaller than 50 microns equivalent spherical diameter in order to separate therefrom mineral impurites, which process comprises the steps of (a) conditioning the fine mineral in the form of an aqueous slurry containing a defloccultant, the aqueous slurry having a solids content in the range 40 to 60 percent by weight, for a time sufficient to dissipate therein at least 25 horsepower hours of energy per ton of mineral solids; (b) mixing the aqueous mineral slurry before or during the conditioning thereof a collector for the mineral impurities; (c) diluting the conditioned mineral slurry to a solids content in the range 15 to 30 percent by weight; (d) introducing the diluted, conditioned mineral slurry into a froth flotation cell having a central, internal, submerged impeller which comprises a base plate, to which there are attached a plurality of blades in radial arrangement, and a stationary cover plate separated from the tips of the blades by a small clearance, the impeller having a diameter which is at least three times its axial height; and (e) subjecting the conditioned aqueous mineral slurry to a pumping action in a froth flotation process which is carried out in the absence of auxiliary carrier particles and without the use of pressurized air and in which the impeller of said froth flotation cell has a peripheral speed of at least 2,500 feet/minute and in which the aeration rate is at least 0.8 cubic feet of air per minute per cubic foot of froth flotation cell volume.