GB900790A - Improvements in or relating to crystalline synthetic cryolite - Google Patents
Improvements in or relating to crystalline synthetic cryoliteInfo
- Publication number
- GB900790A GB900790A GB32850/60A GB3285060A GB900790A GB 900790 A GB900790 A GB 900790A GB 32850/60 A GB32850/60 A GB 32850/60A GB 3285060 A GB3285060 A GB 3285060A GB 900790 A GB900790 A GB 900790A
- Authority
- GB
- United Kingdom
- Prior art keywords
- cryolite
- solution
- fluoride
- sodium aluminate
- saturated
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D9/00—Crystallisation
- B01D9/0036—Crystallisation on to a bed of product crystals; Seeding
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2/00—Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B15/00—Peroxides; Peroxyhydrates; Peroxyacids or salts thereof; Superoxides; Ozonides
- C01B15/055—Peroxyhydrates; Peroxyacids or salts thereof
- C01B15/12—Peroxyhydrates; Peroxyacids or salts thereof containing boron
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01F—COMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
- C01F7/00—Compounds of aluminium
- C01F7/48—Halides, with or without other cations besides aluminium
- C01F7/50—Fluorides
- C01F7/54—Double compounds containing both aluminium and alkali metals or alkaline-earth metals
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01F—COMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
- C01F7/00—Compounds of aluminium
- C01F7/68—Aluminium compounds containing sulfur
- C01F7/74—Sulfates
- C01F7/76—Double salts, i.e. compounds containing, besides aluminium and sulfate ions, only other cations, e.g. alums
- C01F7/762—Ammonium or alkali metal aluminium sulfates
- C01F7/765—Ammonium aluminium sulfates
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Life Sciences & Earth Sciences (AREA)
- Geology (AREA)
- Crystallography & Structural Chemistry (AREA)
- Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
Abstract
<PICT:0900790/III/1> Crystal agglomerates of cryolite are produced by maintaining fine cryolite crystals as a fluidized suspension in an up-flowing super-saturated cryolite solution, whereby agglomerates form and are withdrawn from the suspension. The initial cryolite particles are generally of less than micron size, whilst the agglomerates have a size from 60 to 450 microns and an apparent density from 0,9 to 1,29 grams/c.c. The super-saturated cryolite solution employed may be formed in situ by reaction between sodium aluminate and hydrofluoric acid, sodium fluoride and aluminium fluoride or sulphate, or between ammonium fluoride and sodium aluminate, either in the fluidized bed or in lines leading thereto, for example in the saturated cryolite solution withdrawn from the bed and recycled. As shown in Fig. 1, cryolite crystals of 5 to 20 micron size are introduced from a hopper 5 into a crystallizer 1 through which a recirculated saturated cryolite solution is passed upwardly. Sodium aluminate solution is added to this cryolite solution from a vessel 3 and ammonium fluoride or hydrogen fluoride is passed directly to the crystallizer from a vessel 2. The cryolite crystals are fluidized in the crystallizer 1 and the agglomerates formed are withdrawn through line 7 whilst the supernatant cryolite solution passes through a vessel 6 and cooler 4 for recycle. Cryolite of composition from 5,5 NaF.2AIF3 to 6,87 NaF.2AIF3 may be obtained from sodium aluminate and hydrofluoric acid at pH 2 to 8, or from sodium fluoride and aluminium sulphate at pH 4 to 6, or from ammonium fluoride and sodium aluminate at pH 9,5 to 10,5.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR805954A FR76352E (en) | 1959-09-24 | 1959-09-24 | Process for agglomeration of crystals |
FR826806A FR1264569A (en) | 1960-05-11 | 1960-05-11 | Synthetic Cryolite in Agglomerates |
Publications (1)
Publication Number | Publication Date |
---|---|
GB900790A true GB900790A (en) | 1962-07-11 |
Family
ID=26184428
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB32850/60A Expired GB900790A (en) | 1959-09-24 | 1960-09-23 | Improvements in or relating to crystalline synthetic cryolite |
Country Status (4)
Country | Link |
---|---|
BE (1) | BE572827A (en) |
FR (1) | FR1187352A (en) |
GB (1) | GB900790A (en) |
NL (1) | NL112922C (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2000020335A1 (en) * | 1998-10-05 | 2000-04-13 | Riedel-De Haen Gmbh | Method for the production of complex fluoroaluminate, the fluoroaluminate produced thereby and the utilization of spray drying and polyalkyleneglycols for controlling the structure of fluoroaluminates |
WO2000032739A1 (en) * | 1998-12-03 | 2000-06-08 | Henkel Kommanditgesellschaft Auf Aktien | Granulation method |
US8628733B2 (en) | 2008-11-07 | 2014-01-14 | Areva Nc | Method for preparing uranium concentrates by fluidized bed precipitation, and preparation of UO3 and U3O8 by drying/calcining said concentrates |
CN115028182A (en) * | 2022-06-23 | 2022-09-09 | 多氟多(昆明)科技开发有限公司 | Production facility based on electrolytic aluminum fluorine-containing waste residue manufacturing and processing cryolite |
Families Citing this family (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
BE665905A (en) * | 1964-06-25 | |||
US3666406A (en) * | 1969-09-01 | 1972-05-30 | Showa Denko Kk | Method for manufacturing cryolite with high purity |
US3985862A (en) | 1972-09-02 | 1976-10-12 | Deutsche Gold- Und Silber-Scheideanstalt Vormals Roessler | Process for the production of sodium perborate |
FR2443424A1 (en) * | 1978-12-08 | 1980-07-04 | Ugine Kuhlmann | SODIUM URANATE |
US4530699A (en) * | 1979-01-18 | 1985-07-23 | Aluminum Company Of America | Dense phase precipitation |
FR2508025A1 (en) * | 1981-06-19 | 1982-12-24 | Ugine Kuhlmann | URANIUM PEROXIDE IN THE FORM OF SPHERICAL PARTICLES HAVING GOOD COLORABILITY AND PROCESS FOR OBTAINING THE SAME |
FR2634048B1 (en) * | 1988-07-11 | 1991-04-19 | Pechiney Uranium | PROCESS FOR THE MANUFACTURE OF NUCLEAR FUEL PELLETS COMPRISING THE PRODUCTION AND USE OF SINKING AND SINTERABLE POWDERS OBTAINED DIRECTLY BY PRECIPITATION OF PEROXIDES |
-
1957
- 1957-11-29 FR FR1187352D patent/FR1187352A/en not_active Expired
-
1958
- 1958-11-08 BE BE572827D patent/BE572827A/xx unknown
- 1958-11-28 NL NL233750A patent/NL112922C/xx active
-
1960
- 1960-09-23 GB GB32850/60A patent/GB900790A/en not_active Expired
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2000020335A1 (en) * | 1998-10-05 | 2000-04-13 | Riedel-De Haen Gmbh | Method for the production of complex fluoroaluminate, the fluoroaluminate produced thereby and the utilization of spray drying and polyalkyleneglycols for controlling the structure of fluoroaluminates |
WO2000032739A1 (en) * | 1998-12-03 | 2000-06-08 | Henkel Kommanditgesellschaft Auf Aktien | Granulation method |
US8628733B2 (en) | 2008-11-07 | 2014-01-14 | Areva Nc | Method for preparing uranium concentrates by fluidized bed precipitation, and preparation of UO3 and U3O8 by drying/calcining said concentrates |
CN115028182A (en) * | 2022-06-23 | 2022-09-09 | 多氟多(昆明)科技开发有限公司 | Production facility based on electrolytic aluminum fluorine-containing waste residue manufacturing and processing cryolite |
CN115028182B (en) * | 2022-06-23 | 2022-11-25 | 多氟多(昆明)科技开发有限公司 | Production facility based on electrolytic aluminum fluorine-containing waste residue manufacturing and processing cryolite |
Also Published As
Publication number | Publication date |
---|---|
FR1187352A (en) | 1959-09-10 |
BE572827A (en) | 1958-11-29 |
NL112922C (en) | 1966-06-15 |
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