Production of hydrogen fluoride

Claim 2

A process for the production of the hydrogen fluoride from hydrofluosilicic acid comprising the following steps: a. reacting ammonia with hydrofluosilicic acid to produce an aqueous solution of ammonium fluoride and a precipitate of silica, and separating said silica from said aqueous solution of ammonium fluoride; b. feeding said aqueous solution of ammonium fluoride obtained in step (a) with an alkali metal fluoride, at least partly recycled from step (e), to a continuously operated reactor, wherein said ammonium fluoride and said alkali metal fluoride react to form a bifluoride of said alkali metal in aqueous solution; c. continuously withdrawing reaction mixture from said reactor in step (b), crystallising therefrom a solid product comprising alkali metal bifluoride substantially free from ammonium fluoride, and recycling the mother liquor to said reactor in step (b), the mother liquor comprising a solution of ammonium fluoride, alkali metal fluoride and alkali metal bifluoride thereby obtaining substantially complete conversion of the ammonium fluoride fed to said reactor in step (b) from step (a); d. drying said solid alkali metal bifluoride obtained in step (c) and decomposing at least part of it by heat to produce substantially pure hydrogen fluoride gas and solid alkali metal fluoride; and e. recycling said alkali metal fluoride produced in step (d), together with undecomposed alkali metal bifluoride from step (d), to the reactor in step (b).

Claim 3

A process according to claim 1, in which the conditions of the ammonium fluoride reaction at step (b) are controlled so that the bifluoride ions produced are recoverable from solution as a mixture of alkali metal fluoride and alkali metal bifluoride, in consequence of which said alkali metal fluoride fed to said reactor at step (b) from step (e) is in excess of the amount required to react with said ammonium fluoride fed to said reactor from step (a), the amount of the excess being determined by the proportion of alkali metal fluoride removed with said solid alkali metal bifluoride.

Claim 4

A process according to claim 1, in which the reaction at step (b) is carried out at the boiling point of the reaction mixture thereby facilitating the removal of ammonia and water from said reaction mixture.

Claim 5

A process according to claim 1, in which the molar ratio of fluoride ions to ammonium ions in the reaction mixture at step (b) is maintained 1.7.

Claim 6

A process according to claim 1, in which said solid alkali metal bifluoride is crystallised and separated at a temperature of from 20° to 70° C.

Claim 7

A process for the production of hydrogen fluoride from hydrofluosilicic acid comprising the following steps: a. reacting ammonia with hydrofluosilicic acid to produce an aqueous solution of ammonium fluoride and a precipitate of silica, and separating said silica from said aqueous solution of ammonium fluoride; b. feeding said solution of ammonium fluoride obtained in step (a), and an aqueous mother liquor solution obtained in steps (c) and (d) to a continuously operated reactor, wherein said ammonium fluoride and said potassium fluoride react to form potassium bifluoride in aqueous solution; c. continuously withdrawing reaction mixture from said reactor in step (b), crystallising therefrom a solid product comprising potassium bifluoride and separating from the mother liquor said solid product substantially free from ammonium fluoride, and recycling the mother liquor to said reactor in step (b), the mother liquor comprising a solution of ammonium fluoride, alkali metal fluoride and alkali metal bifluoride, thereby obtaining substantially complete conversion of the ammonium fluoride fed to said reactor in step (b) from step (a); d. mixing at least part of said solid potassium bifluoride obtained at step (c) with sodium fluoride recycled from step (f), in the presence of water in a reactor to form solid sodium bifluoride and an aqueous solution of potassium fluoride, separating said solid sodium bifluoride from the mother liquor, and recycling said mother liquor to said reactor at step (b); e. drying said solid sodium bifluoride from step (d) and decomposing at least part of it by heat to produce substantially pure hydrogen fluoride gas and solid sodium fluoride; and f. recycling said solid sodium fluoride produced at step (e), together with undecomposed sodium bifluoride from step (e), to said reactor at step (d).

Claim 8

A process for the production of hydrogen fluoride from hydrofluosilicic acid comprising the following steps: a. reacting ammonia with hydrofluosilicic acid to produce an aqueous solution of ammonium fluoride and a precipitate of silica, and separating said silica from said aqueous solution of ammonium fluoride; b. feeding said solution of ammonium fluoride obtained in step (a), and an aqueous mother liquor solution obtained in steps (c) and (d) to a continuously operated reactor, wherein said ammonium fluoride and said potassium fluoride react to form potassium bifluoride in aqueous solution; c. continuously withdrawing reaction mixture from said reactor in step (b), crystallising therefrom a solid product comprising potassium bifluoride and separating from the mother liquor said solid product substantially free from ammonium fluoride, and recycling the mother liquor to said reactor in step (b), the mother liquor comprising a solution of ammonium fluoride, alkali metal fluoride and alkali metal bifluoride, thereby obtaining substantially complete conversion of the ammonium fluoride fed to said reactor in step (b) from step (a); d. mixing at least part of said solid potassium bifluoride obtained at step (c) with sodium fluoride recycled from step (f), in the presence of water in a reactor to form solid sodium bifluoride and an aqueous solution of potassium fluoride, separating said solid sodium bifluoride from the mother liquor, and recycling said mother liquor to said reactor at step (b); e. drying said solid sodium bifluoride from step (d) and decomposing at least part of it by heat to produce substantially pure hydrogen fluoride gas and solid sodium fluoride; and f. recycling said solid sodium fluoride produced at step (e), together with undecomposed sodium bifluoride from step (e), to said reactor at step (d).

Claim 9

A process according to claim 6, in which the conditions of the ammonium fluoride reaction at step (b) are controlled so that the bifluoride ions produced are recoverable from solution as a mixture of potassium fluoride and potassium bifluoride, in consequence of which the potassium fluoride fed to said reactor at step (b) from step (d) is in excess of the amount required to react with said ammoniuly fluoride fed to said reactor from step (a), the amount of the excess being determined by the proportion of potassium fluoride removed with said solid potassium bifluoride.

Claim 10

A process according to claim 6, in which the reaction at step (b) is carried out at the boiling point of the reaction mixture, thereby facilitating the removal of ammonia and water from said reaction mixture.

Claim 11

A process according to claim 6, in which said solid sodium bifluoride produced at step (d) is produced as a mixture of sodium bifluoride and sodium fluoride.

Claim 12

A process according to claim 6, in which said aqueous solution of potassium fluoride produced at step (d) also contains potassium bifluoride, said aqueous solution being recycled to said reactor at step (b).

Claim 13

A process for the production of the hydrogen fluoride from hydrofluosilicic acid comprising the following steps: a. reacting ammonium with hydrofluosilicic acid to produce an aqueous solution of ammonium fluoride and a precipitate of silica, and separating said silica from said aqueous solution of ammonium fluoride; b. feeding said aqueous solution of ammonium fluoride obtained in step (a) with a potassium fluoride, at least partly recycled from step (e), to a continuously operated reactor, wherein said ammonium fluoride and said potassium fluoride react to form a potassium bifluoride in aqueous solution; c. continuously withdrawing reaction mixture from said reactor in step (b) crystallising therefrom a solid product comprising potassium bifluoride substantially free from ammonium fluoride, and recycling the mother liquor to said reactor in step (b), the mother liquor comprising a solution of ammonium fluoridie, alkali metal metal fluoride and alkali metal bifluoride, thereby obtaining substantially complete conversion of the ammonium fluoride fed to said reactor in step (b) from step (a); d. drying said solid potassium bifluoride obtained in step (c) and decomposing at least part of it by heat to produce substantially pure hydrogen fluoride gas and solid potassium fluoride; and e. recycling said potassium fluoride produced in step (d), together with undecomposed potassium bifluoride from step (d), to the reactor in step (b).

Claim 14

A process for the production of the hydrogen fluoride from hydrofluosilicic acid comprising the following steps: a. reacting ammonium with hydrofluosilicic acid to produce an aqueous solution of ammonium fluoride and a precipitate of silica, and separating said silica from said aqueous solution of ammonium fluoride; b. feeding said aqueous solution of ammonium fluoride obtained in step (a) with a potassium fluoride, at least partly recycled from step (e), to a continuously operated reactor, wherein said ammonium fluoride and said potassium fluoride react to form a potassium bifluoride in aqueous solution; c. continuously withdrawing reaction mixture from said reactor in step (b) crystallising therefrom a solid product comprising potassium bifluoride substantially free from ammonium fluoride, and recycling the mother liquor to said reactor in step (b), the mother liquor comprising a solution of ammonium fluoridie, alkali metal metal fluoride and alkali metal bifluoride, thereby obtaining substantially complete conversion of the ammonium fluoride fed to said reactor in step (b) from step (a); d. drying said solid potassium bifluoride obtained in step (c) and decomposing at least part of it by heat to produce substantially pure hydrogen fluoride gas and solid potassium fluoride; and e. recycling said potassium fluoride produced in step (d), together with undecomposed potassium bifluoride from step (d), to the reactor in step (b).