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US3887693A Expired / Lapsed US ⏱️ 0.0 years remaining

Continuous process for obtaining aluminium fluoride by reacting fluosilicic acid with an aluminous material

Assignee: Derivados del Fluor SA
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Filing: 1973-05-25
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Granted: 1975-06-03
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Expires: 1993-05-25
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Abstract

Abstract The present invention relates to a continuous process for preparing aluminium fluoride by reacting fluosilicic acid (substantially pure) obtained from superphosphate, phosphoric acid or hydrofluoric acid industries, having a maximum P2O5 content of 250 ppm and an aluminous material, preferably alumina or bauxite hydrate.

Inventors

  • 👤 Nevado Antonio Escribano
  • 👤 Lago Eduardo Chapela
  • 👤 Hernandez Jesus Gutierrez

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-30 13:43
CPC Classifications
C; C01; C01B; C01B33/00; C01B33/113; C01B33/12; C01B33/18; C01B33/186; C01F; C01F7/00; C01F7/48; C01F7/50; C01P; C01P2006/00; C01P2006/80

Claims Analysis

Total Claims: 14
Claim 1
Independent Claim 194 words
Continuous process for obtaining aluminum fluoride by reacting fluosiliCic acid with an aluminous material, forming a suspension of insoluble silica hydrate and a supersaturated solution of Alpha -allotropic aluminum fluoride, which reaction is carried out by using fluosilicic acid having a concentration of 5 to 25%, previously heated to approximately 60* to 95*C, and finely pulverized alumina or bauxite hydrate high in silica; the reaction mixture being maintained at a temperature above 90*C, for a reaction time from 5 to 60 minutes, the process being carried out continuously in a battery of reactors arranged in cascade, the reaction being effected progressively from the first to the last reactor; the reaction flow being uniform; and the reactants being continuously introduced through the first reactor uniformly and continuously in such amount that the suspension emerging from the last reactor is maintained at a pH between 1 and 3, the insoluble silica hydrate being separated from said suspension which emerges from the last reactor, while said supersaturated Alpha -allotropic aluminum fluoride solution obtained is lead to a battery of crystallizers, arranged in cascade, where the Alpha -aluminum fluoride is continuously converted to its insoluble Beta -allotropic state.
Claim 2
Dependent Claim 194 words
Continuous process for obtaining aluminum fluoride by reacting fluosiliCic acid with an aluminous material, forming a suspension of insoluble silica hydrate and a supersaturated solution of Alpha -allotropic aluminum fluoride, which reaction is carried out by using fluosilicic acid having a concentration of 5 to 25%, previously heated to approximately 60* to 95*C, and finely pulverized alumina or bauxite hydrate high in silica; the reaction mixture being maintained at a temperature above 90*C, for a reaction time from 5 to 60 minutes, the process being carried out continuously in a battery of reactors arranged in cascade, the reaction being effected progressively from the first to the last reactor; the reaction flow being uniform; and the reactants being continuously introduced through the first reactor uniformly and continuously in such amount that the suspension emerging from the last reactor is maintained at a pH between 1 and 3, the insoluble silica hydrate being separated from said suspension which emerges from the last reactor, while said supersaturated Alpha -allotropic aluminum fluoride solution obtained is lead to a battery of crystallizers, arranged in cascade, where the Alpha -aluminum fluoride is continuously converted to its insoluble Beta -allotropic state.
Claim 3
Dependent Claim 137 words
CONTINUOUS PROCESS FOR OBTAINING ALUMINUM FLUORIDE BY REACTING FLUOSILICIC ACID WITH AN ALUMINOUS MATERIAL, FORMING A SUSPENSION OF INSOLUBLE SILICA HYDRATE AND A SUPERSATURATED SOLUTION OF A-ALLOTROPIC ALUMINUM FLUORIDE, WHICH REACTION IS CARRIED OUT BY USING FLUOSILICIC ACID HAVING A CONCENTRATION OF 5 TO 25%, PREVIOUSLY HEATED TO APPROXIMATELY 60* TO 95*C. AND FINELY PULVERIZED ALUMINA OR BAUXITE HYDRATE HIGH IN SILICA; THE REACTION MIXTURE BEING MAINTAINED AT A TEMPERATURE ABOVE 90*C, FOR A REACTION TIME FROM 5 TO 60 MINUTES, THE PROCESS BEING CARRIED OUT CONTINUOUSLY IN A BATTERY OF REACTORS ARRANGED IN CASCADE, THE REACTION BEING EFFECTED PROGRESSIVELY FROM THE FIRST TO THE LAST REACTOR; THE REACTION FLOW BEING UNIFORM; AND THE REACTANTS BEING CONTINUOUSLY INTRODUCED THROUGH THE FIRST REACTOR UNIFORMLY AND CONTINUOUSLY IN SUCH AMOUNT THAT THE SUSPENSION EMERGING FROM THE LAST REACTOR IS
Claim 4
Dependent Claim 137 words
CONTINUOUS PROCESS FOR OBTAINING ALUMINUM FLUORIDE BY REACTING FLUOSILICIC ACID WITH AN ALUMINOUS MATERIAL, FORMING A SUSPENSION OF INSOLUBLE SILICA HYDRATE AND A SUPERSATURATED SOLUTION OF A-ALLOTROPIC ALUMINUM FLUORIDE, WHICH REACTION IS CARRIED OUT BY USING FLUOSILICIC ACID HAVING A CONCENTRATION OF 5 TO 25%, PREVIOUSLY HEATED TO APPROXIMATELY 60* TO 95*C. AND FINELY PULVERIZED ALUMINA OR BAUXITE HYDRATE HIGH IN SILICA; THE REACTION MIXTURE BEING MAINTAINED AT A TEMPERATURE ABOVE 90*C, FOR A REACTION TIME FROM 5 TO 60 MINUTES, THE PROCESS BEING CARRIED OUT CONTINUOUSLY IN A BATTERY OF REACTORS ARRANGED IN CASCADE, THE REACTION BEING EFFECTED PROGRESSIVELY FROM THE FIRST TO THE LAST REACTOR; THE REACTION FLOW BEING UNIFORM; AND THE REACTANTS BEING CONTINUOUSLY INTRODUCED THROUGH THE FIRST REACTOR UNIFORMLY AND CONTINUOUSLY IN SUCH AMOUNT THAT THE SUSPENSION EMERGING FROM THE LAST REACTOR IS
Claim 5
Dependent Claim 40 words
Continuous process for obtaining aluminum fluoride by reacting fluosilicic acid with an aluminous material, according to claim 1 characterized in that the number of reactors ranges between 2 and 6, each reactor having its own controllable heating and agitating elements.
Claim 6
Dependent Claim 32 words
Continuous process for obtaining aluminum fluoride by reacting fluosilicic acid with an aluminous material according to claim 1, characterized in that the residence time in each reactor is less than 5 minutes.
Claim 7
Dependent Claim 39 words
Continuous process for obtaining aluminum fluoride by reacting fluosilicic acid with an aluminous material according to claim 1, characterized in that said suspension is centrifuged and the silica cake of each centrifugation is washed in one or several stages.
Claim 8
Dependent Claim 37 words
Continuous process for obtaining aluminum fluoride by reacting fluosilicic acid with an aluminous material according to claim 1, characterized in that said suspension is diluted with pure water, with wash liquors or with a mixture of both.
Claim 9
Dependent Claim 31 words
A continuous process according to claim 1 wherein the fluosilicic acid or aluminous material is added to any one of the reactor cascades in determined amounts to adjust the pH rapidly.
Claim 10
Dependent Claim 16 words
A continuous process according to claim 1 wherein the fluosilicic acid has a concentration of 16%.
Claim 11
Dependent Claim 14 words
A continuous process according to claim 1 wherein the reaction time is 15 minutes.
Claim 12
Dependent Claim 24 words
A continuous process according to claim 2 wherein the number of crystallizers is 4, each crystallizer having its own controllable heating and agitating elements.
Claim 13
Dependent Claim 16 words
A continuous process according to claim 1 wherein the reaction is performed at the boiling point.
Claim 14
Dependent Claim 91 words
A continuous process according to claim 4 wherein when the washing is carried out in several stages, clean, warm water is used in the last stage and the solution thus obtained is used as the wash liquor for the penultimate step of a subsequent wash cycle and this, in turn, serves as the wash liquor for the second last step of a further subsequent wash cycle, and so on, successively until finally, the liquid coming from the first washing stage is added to said supersaturated solution of allotropic Alpha -aluminum fluoride.

References Cited (Backward Citations)

US2527340A Cited
US2664341A Cited
US2920938A Cited
US2842426A Cited
US2958575A Cited
US3057681A Cited
US3175882A Cited
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USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1978-06-02 1978-12-02 1979-06-03 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1982-06-02 1982-12-02 1983-06-03 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1986-06-02 1986-12-02 1987-06-03 $7700.00 Window Closed / Lapsed

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