Process for producing columbium oxyfluoride

Claim 2

A process for the production of columbium oxyfluoride comprising; heating to boiling in a reactor, with agitation, an aqueous feed solution containing hydrofluoric acid and dissolved columbium to thereby cause evaporation and hydrolysis of the aqueous feed solution to occur resulting in the formation of a columbium oxyfluoride-containing slurry, said agitation sufficient to maintain the hydrolyzed product in suspension; and recovering the columbium oxyufluoride from the slurry, as formed, by separating the columbium oxyfluoride from the liquid phase of the slurry.

Claim 3

The process as defined in claim 1 wherein the solution is heated to a temperature of at least about 100° C.

Claim 4

The process as defined in claim 1 wherein the solution is heated to a temperature ranging from at least about 100° C. to about 180° C.

Claim 5

The process as defined in claim 1 wherein the solution is heated to a temperature ranging from about 150° C. to about 160° C.

Claim 6

The process as defined in claim 1 wherein the aqueous feed solution contains dissolved columbium in an amount ranging from about 25 to about 700 g/L.

Claim 7

The process as defined in claim 1 wherein the aqueous feed solution contains dissolved columbium in an amount ranging from about 250 to about 600 g/L.

Claim 8

The process as defined in claim 1 wherein the aqueous feed solution contains dissolved columbium in an amount of about 500 g/L.

Claim 9

The process as defined in claim 1 wherein the aqueous feed solution contains hydrofluoric acid and dissolved columbium in amounts such that the molar ratio of fluorine to columbium in the aqueous feed solution is at least 4.

Claim 10

The process as defined in claim 1 wherein the aqueous feed solution contains hydrofluoric acid and dissolved columbium in amounts such that the molar ratio of fluorine to columbium in the aqueous feed solution is at least 4.5.

Claim 11

The process as defined in claim 1 wherein the aqueous feed solution contains hydrofluoric acid and dissolved columbium in amounts such that the molar ratio of fluorine to columbium in the aqueous feed solution is about 5.5 to about 6.0.

Claim 12

A process for the production of columbium oxyfluoride comprising: (a) heating to boiling in a reactor, with agitation, an aqueous feed solution containing hydrofluoric acid and dissolved columbium to thereby cause evaporation and hydrolysis of the aqueous feed solution to occur resulting in the formation of a columbium oxyfluoride-containing slurry, said agitation sufficient to maintain the hydrolyzed product in suspension; (b) recovering the columbium oxyfluoride from a portion of the slurry, as formed, by separating the columbium oxyfluoride from the liquid phase of the slurry portion; (c) recycling the resulting separated liquid phase to the reactor; and (d) introducing additional aqueous feed solution to the reactor at a rate sufficient to maintain a suitable volume of slurry and to prevent the slurry from evaporating to dryness.

Claim 13

A process for the production of columbium oxyfluoride comprising: (a) heating to boiling in a reactor, with agitation, an aqueous feed solution containing hydrofluoric acid and dissolved columbium to thereby cause evaporation and hydrolysis of the aqueous feed solution to occur resulting in the formation of a columbium oxyfluoride-containing slurry, said agitation sufficient to maintain the hydrolyzed product in suspension; (b) recovering the columbium oxyfluoride from a portion of the slurry, as formed, by separating the columbium oxyfluoride from the liquid phase of the slurry portion; (c) recycling the resulting separated liquid phase to the reactor; and (d) introducing additional aqueous feed solution to the reactor at a rate sufficient to maintain a suitable volume of slurry and to prevent the slurry from evaporating to dryness.

Claim 14

The process of claim 11 wherein the columbium oxyfluoride is continuously recovered from a portion of the slurry and additional aqueous feed solution is continuously introduced to the reactor at a rate sufficient to maintain a suitable volume of slurry.

Claim 15

The process as defined in claim 11 wherein the solution is heated to a temperature of at least about 100° C.

Claim 16

The process as defined in claim 11 wherein the solution is heated to a temperature ranging from at least about 100° C. to about 180° C.

Claim 17

The process as defined in claim 11 wherein the solution is heated to a temperature ranging from about 150° C. to about 160° C.

Claim 18

The process as defined in claim 11 wherein the aqueous feed solution contains dissolved columbium in an amount ranging from about 25 to about 700 g/L.

Claim 19

The process as defined in claim 11 wherein the aqueous feed solution contains dissolved columbium in an amount ranging from about 250 to about 600 g/L.

Claim 20

The process as defined in claim 11 wherein the aqueous feed solution contains dissolved columbium in an amount of about 500 g/L.

Claim 21

The process as defined in claim 11 wherein the aqueous feed solution contains hydrofluoric acid and dissolved columbium in amounts such that the molar ratio of fluorine to columbium in the aqueous feed solution is at least 4.

Claim 22

The process as defined in claim 11 wherein the aqueous feed solution contains hydrofluoric acid and dissolved columbium in amounts such that the molar ratio of fluorine to columbium in the aqueous feed solution is at least 4.5.

Claim 23

The process as defined in claim 11 wherein the aqueous feed solution contains hydrofluoric acid and dissolved columbium in amounts such that the molar ratio of fluorine to columbium in the aqueous feed solution is about 5.5 to about 6.0.