PROCESSES FOR TREATING ELECTROLYTE FROM AN ELECTROREFINING PROCESS

1 .- 36 . (canceled)

37 . A process for treating an aqueous solution including impurity material disposed in a first state, comprising:

modifying the state of the impurity material, disposed in the first state, from the first state to the second state, such that a conditioned aqueous solution, including the modified impurity material, is obtained; and

contacting the conditioned aqueous solution with an operative sorptive media with effect that at least a portion of the modified impurity material becomes sorbed to the operative sorptive media, such that an impurity material-depleted aqueous solution is produced.

38 . The process as claimed in claim 37 ;

wherein the modifying of the state of the impurity material is with effect that affinity of the impurity material to the operative sorptive media is decreased.

39 . The process as claimed in claim 37 ;

wherein the modifying of the state of the impurity material includes a change to the oxidation state of the impurity material.

40 . The process as claimed in claim 37 ;

wherein the modifying of the state of the impurity material is effected by a reduction of the first state of the impurity material.

41 . The process as claimed in claim 37 ;

wherein the sorption of the modified impurity material to the operative sorptive media is effected in response to an exchange of material between the modified impurity material of the aqueous solution and an exchangeable material of the operative sorptive media; and

the exchange of material includes an exchange of ions, such that the operative sorptive media includes ion exchange material.

42 . The process as claimed in claim 41 ;

wherein:

the ion exchange material is disposed within a contacting zone; and

the contacting of the conditioned aqueous solution with an operative sorptive media includes supplying the conditioned aqueous material to the contacting zone such that a contacting zone material becomes disposed within the contacting zone, and while the supplying is being effected, discharging the contacting zone material from the contacting zone with effect that the impurity material-depleted aqueous solution is obtained, and the residence time of the contacting zone material within the contacting zone is at least three (3) seconds.

43 . The process as claimed in claim 37 ;

further comprising:

electrorefining a target metal within an electrolysis cell;

bleeding a portion of the electrolyte from the electrolysis cell;

wherein the aqueous solution is defined by the bleed.

44 . The process as claimed in claim 43 ;

further comprising, after the impurity material-depleted aqueous solution has been produced:

supplying the electrolysis cell with the impurity material-depleted aqueous solution.

45 . The process as claimed in claim 37 ;

wherein:

the impurity material is arsenic;

the first state of arsenic is arsenic (V); and

the second state of arsenic is arsenic (III).

46 . The process as claimed in claim 45 ;

wherein the modifying of the impurity material includes contacting the aqueous solution with a reducing agent within a reaction zone.

47 . The process as claimed in claim 46 ;

wherein the reducing agent is sulphur dioxide.

48 . The process as claimed in claim 47 ;

wherein the ratio of moles of sulphur dioxide to the moles of arsenic (V) is at least 1:1.

49 . The process as claimed in claim 47 ;

wherein the contacting of the aqueous material with the reducing agent within the reaction zone includes supplying the aqueous material and the reducing agent to the reaction zone such that a reaction zone material becomes disposed within the reaction zone, and while the supplying is being effected, discharging the reaction zone material from the reaction zone with effect that the conditioned aqueous material is produced, and the residence time of the reaction zone material within the reaction zone is at least 15 minutes.

50 . The process as claimed in claim 47 ;

wherein:

the impurity material-depleted aqueous solution includes sulphur dioxide;

and further comprising, after the impurity material-depleted aqueous solution has been produced:

converting the sulphur dioxide to sulphuric acid.

51 . The process as claimed in claim 50 ;

wherein the aqueous solution includes sulphuric acid.

52 . The process as claimed in claim 45 ;

further comprising:

electrorefining a target metal within an electrolysis cell;

bleeding a portion of the electrolyte from the electrolysis cell;

wherein the aqueous solution is defined by the bleed.

53 . The process as claimed in claim 51 ;

further comprising, after the impurity material-depleted aqueous solution has been produced:

supplying the electrolysis cell with the impurity material-depleted aqueous solution.

54 . The process as claimed in claim 51 ;

wherein the target metal is copper.

55 . A process for treating a feed material with a reagent, comprising;

emplacing a reaction zone discharge in selective mass transfer communication with the feed material such that reagent material is transferred from the reaction zone discharge to the feed material, with effect that a modified feed material is obtained that is augmented with the transferred reagent material;

contacting the modified feed material with an adscititious reagent material within a reaction zone, such that a reactive process is effected to produce a reaction product, and such that a reaction zone material becomes disposed in the reaction zone and includes the reaction product and residual reagent material; and

discharging the reaction zone material from the reaction zone;

wherein the discharged reaction zone material defines the reaction zone discharge.

56 . The process as claimed in claim 55 ;

wherein the contacting includes admixing of the modified feed material and the adscititious reagent material.

57 . The process as claimed in claim 55 ;

wherein the adscititious reagent material is supplied to the reaction zone from a reagent material supply source.