Control system for froth flotation processes

Claim 2

A method according to claim 1 wherein said time lapse approximates to the time taken for slurry to pass through the system between input and output sensing locations.

Claim 3

A method according to claim 1 wherein the solids contents in said streams are sensed by measuring turbidity of samples withdrawn from the streams.

Claim 4

A method according to claim 3 wherein said samples are diluted by addition of water to reduce the solids contents of each sample in proportion to levels readable by turbidity measuring apparatus.

Claim 5

A method according to claim 4 wherein the maximum solids content of said samples to reduced to about 2%.

Claim 6

A method according to claim 4 wherein said samples are continuously flowing and in which the rate of flow is maintained substantially constant.

Claim 7

A method according to claim 2 wherein readjustment of reagent dosage is effected at intervals of less than one minute.

Claim 8

A method according to claim 1 wherein the ash content in said frothed product is also monitored and the reagent dosage adjusted to maintain the ash content within predetermined limits.

Claim 9

Apparatus for monitoring the operation of a froth flotation process having an input stream consisting of raw feed, a first output stream consisting of frothed product to be reclaimed and a second output stream consisting of tailings to be discarded, the apparatus comprising means for assessing the solids content of said input stream, control means operable in response to signals derived from said assessment to vary the dosage of flotation reagent employed in the process, means for assessing the solids content of at least one of said output streams after a predetermined time lapse, comparator means adapted to receive signals generated in response to said assessments and to compare same with control data relating input and output solids content and to generate a control signal dependent on said comparison, and said control means being operable in response to said control signal to effect compensating readjustment of the dosage of flotation reagent employed in the process.

Claim 10

Apparatus according to claim 9 wherein said time lapse approximates to the time taken for slurry to pass through the system between input and output assessment locations.

Claim 11

Apparatus according to claim 9 including means for withdrawing samples from said streams and directing same to said means for assessing solids content.

Claim 12

Apparatus according to claim 11 wherein said means for withdrawing samples includes take-off pipes which are provided with flow control means.

Claim 13

Apparatus according to claim 12 wherein said flow control means comprise metering pumps.

Claim 14

Apparatus according to claim 11 including means for diluting said samples prior to delivery to said means for assessing solids content.

Claim 15

Apparatus according to claim 14 wherein each of said means for diluting said samples and each means for assessing the solids content are combined to form a sensing unit including a dilution water inlet and a sample inlet connected to a mixing chamber.

Claim 16

Apparatus according to claim 15 wherein said means for assessing the solids content of said input and output streams comprises turbidity measuring means.

Claim 17

Apparatus according to claim 16 wherein said turbidity measuring means is located adjacent the outlet from said mixing chamber.

Claim 18

Apparatus according to claim 17 wherein said turbidity measuring means incorporates a light emitting device and a light sensitive cell between which the diluted sample passes, said light sensitive cell producing an output signal dependent on the light intensity sensed by the cell and hence related to the solids content of the sample.

Claim 19

Apparatus according to claim 15 including a common discharge pipe connected to all of said sensing units and arranged to return the discharged samples to said input stream.

Claim 20

Apparatus according to claim 9 wherein said comparator means comprises a computer.

Claim 21

Apparatus according to claim 18 wherein said comparator means comprises a computer and each of said sensing units is electrically connected to said computer to transmit each of said output signals thereto.

Claim 22

Apparatus according to claim 20 or 21 wherein said flotation reagents are added to the raw feed by metering means operation of which is controlled by output signals from said computer.

Claim 23

Apparatus according to claim 9 including additional assessment means to determine ash content in the frothed product.

Claim 24

Apparatus according to claim 23 wherein said additional sensing means is adapted to transmit control signals to said computer operable to vary the dosage of flotation reagent to maintain ash level in the frothed product between predetermined parameters.