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US3968197A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for treating sodium silico fluoride

Assignee: Onoda Chemical Industry Co Ltd
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Filing: 1974-08-08
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Granted: 1976-07-06
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Expires: 1994-08-08
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Abstract

Abstract The invention relates to a process of the treatment of sodium silico fluoride. In the invention, sodium silico fluoride is decomposed with a relatively high concentration of an aqueous ammonium solution or an ammonia gas to produce a mixed aqueous slurry solution of ammonium fluoride containing sodium fluoride and silica gels as solid materials, the obtained mixed aqueous slurry solution is separated to the ammonium fluoride solutions containing sodium fluoride and silica gels, respectively, by means of a physical method and then sodium fluoride, silica gels and the aqueous ammonium fluoride solution are manufactured in high purity and good yield, respectively. In the other way, the mixture of sodium fluoride and silica gels are separated from said mixed aqueous slurry solution by means of the filter, washed with water and dried. The dried mixture is separated to sodium fluoride and silica gels by means of a physical method. Further, ammonium fluoride in the mixed aqueous slurry solution manufactured according to said process may be decomposed with sodium hydroxide or sodium salt to sodium fluoride and an ammonium or ammonium salts solution to be used.

Inventors

  • 👤 Hirokazu Satoh
  • 👤 Akira Fujimura

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-09 04:01
CPC Classifications
C; C01; C01C; C01C1/00; C01C1/16; C01C1/162; C01B; C01B33/00; C01B33/113; C01B33/12; C01B33/14; C01B33/152; C01B33/1525; C01D; C01D1/00; C01D1/04; C01D1/20; C01D1/24; C01D3/00; C01D3/02

Claims Analysis

Total Claims: 5
Claim 1
Independent Claim 232 words
In the process of reacting sodium silicofluoride having a particle size of less than 250 microns and ammonia in an aqueous medium to produce silica, sodium fluoride and ammonium fluoride, the improvement comprising: a. adding ammonia, in the form of a member selected from the group consisting of free ammonia gas and aqueous ammonium hydroxide having a concentration, calculated as free ammonia, of at least about 7.5 weight percent, at a rate such that the concentration of ammonium hydroxide in the reaction medium is less than about 5 weight percent over a period of at least about 60 minutes, until substantially all the sodium silicofluoride is reacted: b. agitating to a degree greater than that required to disperse sodium fluoride crystals and silica gel of said reaction medium produced in the course of said addition of ammonia and for a period of at least about 20 minutes after completion of said addition of ammonia: c. after completion of the reaction, adding a stoichiometric excess of said ammonia in an amount such that the total ammonium ion concentration consisting of ammonium fluoride and ammonium hydroxide in the reaction medium is more than 7.5 weight percent, calculated as free ammonia; and d. separating sodium fluoride crystals having a particle size of more than 100 microns and silica gel having a particle size of less than 5 microns thus prepared separately from ammonium fluoride solution.
Claim 2
Dependent Claim 232 words
In the process of reacting sodium silicofluoride having a particle size of less than 250 microns and ammonia in an aqueous medium to produce silica, sodium fluoride and ammonium fluoride, the improvement comprising: a. adding ammonia, in the form of a member selected from the group consisting of free ammonia gas and aqueous ammonium hydroxide having a concentration, calculated as free ammonia, of at least about 7.5 weight percent, at a rate such that the concentration of ammonium hydroxide in the reaction medium is less than about 5 weight percent over a period of at least about 60 minutes, until substantially all the sodium silicofluoride is reacted: b. agitating to a degree greater than that required to disperse sodium fluoride crystals and silica gel of said reaction medium produced in the course of said addition of ammonia and for a period of at least about 20 minutes after completion of said addition of ammonia: c. after completion of the reaction, adding a stoichiometric excess of said ammonia in an amount such that the total ammonium ion concentration consisting of ammonium fluoride and ammonium hydroxide in the reaction medium is more than 7.5 weight percent, calculated as free ammonia; and d. separating sodium fluoride crystals having a particle size of more than 100 microns and silica gel having a particle size of less than 5 microns thus prepared separately from ammonium fluoride solution.
Claim 3
Dependent Claim 26 words
The process of claim 1 wherein said member is aqueous ammonium hydroxide having a concentration, calculated as free ammonia, of about 15 to 45 weight percent.
Claim 4
Dependent Claim 53 words
The process of claim 1 wherein said ammonium fluoride is reacted with a member selected from the first group consisting of sodium hydroxide, sodium chloride, and sodium sulfate to produce sodium fluoride and an aqueous solution of the corresponding member selected from the second group consisting ammonium hydroxide, ammonium chloride, and ammonium sulfate.
Claim 5
Dependent Claim 29 words
The process of claim 3 wherein the member selected from said first group is added as an aqueous solution having a concentration of at least about 10 weight percent.

References Cited (Backward Citations)

US3021194A Cited
US3563699A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1979-07-06 1980-01-05 1980-07-06 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1983-07-06 1984-01-05 1984-07-06 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1987-07-06 1988-01-05 1988-07-06 $7700.00 Window Closed / Lapsed

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