US3887693A
Expired / Lapsed
US
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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
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.
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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 |