GB668612A - Method of producing coarsely crystalline sodium carbonate monohydrate - Google Patents
Method of producing coarsely crystalline sodium carbonate monohydrateInfo
- Publication number
- GB668612A GB668612A GB19830/50A GB1983050A GB668612A GB 668612 A GB668612 A GB 668612A GB 19830/50 A GB19830/50 A GB 19830/50A GB 1983050 A GB1983050 A GB 1983050A GB 668612 A GB668612 A GB 668612A
- Authority
- GB
- United Kingdom
- Prior art keywords
- water
- sodium carbonate
- steam
- per cent
- soda
- 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
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01D—COMPOUNDS OF ALKALI METALS, i.e. LITHIUM, SODIUM, POTASSIUM, RUBIDIUM, CAESIUM, OR FRANCIUM
- C01D7/00—Carbonates of sodium, potassium or alkali metals in general
- C01D7/35—Varying the content of water of crystallisation or the specific gravity
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Inorganic Chemistry (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
Abstract
Coarsely crystalline sodium carbonate monohydrate is produced by mixing sodium carbonate from the ammonia soda process, preferably immediately after calcination and while still hot, with the water required for the formation of the monohydrate, e.g. 20-50 per cent preferably in the form of steam, the mass being kept in motion at 70 DEG C. while maintaining the water content, suitably by working in a closed apparatus. Excess water is preferably used which may be removed by passing a current of warm air over the mass at completion. The resulting coarse grained monohydrate may be calcined at about 130 DEG C. to give coarse grained sodium carbonate. An example relates to the treatment of calcined ammonia-soda with steam in a closed rotating drum until 20 per cent of water has been absorbed. The temperature rises to 105 DEG C., the steam is cut off and the temperature maintained between 90 DEG -100 DEG C. for 50 minutes. Air is passed over at 40 DEG -60 DEG C. to remove excess water. A further example relates to treatment with water at 80 DEG C. It is stated in the Specification to be known that granulated dense soda may be produced by mixing soda of low bulk density with 16 per cent of water in a screw mixer and subsequently drying at 135 DEG -190 DEG C., the steam from the drier being condensed and recycled to provide the 16 per cent of water required for hydration.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE668612X | 1949-08-16 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB668612A true GB668612A (en) | 1952-03-19 |
Family
ID=6590062
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB19830/50A Expired GB668612A (en) | 1949-08-16 | 1950-08-09 | Method of producing coarsely crystalline sodium carbonate monohydrate |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB668612A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1008721B (en) * | 1953-11-02 | 1957-05-23 | Diamond Alkali Co | Process for the production of alkali carbonates, in particular anhydrous soda, of a predetermined, relatively low bulk weight |
US3309171A (en) * | 1966-02-11 | 1967-03-14 | Intermountain Res & Dev Corp | Densification of soda ash by vapor hydration |
JPS5050298A (en) * | 1973-09-05 | 1975-05-06 |
-
1950
- 1950-08-09 GB GB19830/50A patent/GB668612A/en not_active Expired
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1008721B (en) * | 1953-11-02 | 1957-05-23 | Diamond Alkali Co | Process for the production of alkali carbonates, in particular anhydrous soda, of a predetermined, relatively low bulk weight |
US3309171A (en) * | 1966-02-11 | 1967-03-14 | Intermountain Res & Dev Corp | Densification of soda ash by vapor hydration |
JPS5050298A (en) * | 1973-09-05 | 1975-05-06 | ||
JPS532440B2 (en) * | 1973-09-05 | 1978-01-27 |
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