GB882694A - Purification of sodium carbonate - Google Patents
Purification of sodium carbonateInfo
- Publication number
- GB882694A GB882694A GB37969/57A GB3796957A GB882694A GB 882694 A GB882694 A GB 882694A GB 37969/57 A GB37969/57 A GB 37969/57A GB 3796957 A GB3796957 A GB 3796957A GB 882694 A GB882694 A GB 882694A
- Authority
- GB
- United Kingdom
- Prior art keywords
- sodium carbonate
- slurry
- monohydrate
- unhydrated
- weight
- 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
- C01D7/22—Purification
- C01D7/24—Crystallisation
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Inorganic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
<PICT:0882694/III/1> Sodium carbonate is purified by cooling a slurry of unhydrated solid sodium carbonate from a temperature above 112 DEG C. to below 112 DEG C. but not less than 32 DEG C. thereby forming an aqueous slurry of solid sodium carbonate monohydrate which is separated to produce a pure product. The initial slurry of unhydrated sodium carbonate is preferably prepared by forming a slurry of sodium carbonate monohydrate, heating to above 112 DEG C. and generally from 115-150 DEG C. to convert the monohydrate to the unhydrated salt and thereafter cooling to below 112 DEG C. as above. In order to prevent coalescence it is preferable to keep the solids content of the slurry below 75% by weight during cooling. As shown in the Figure, crude soda ash was slurried in water and treated in tank 10 with elemental chlorine to improve the colour and then pumped to a reactor 18 where the slurry is heated above the transition point from the monohydrate to the unhydrated salt (112 DEG C.) and preferably at 120 DEG C. for about five minutes. The slurry of anhydrous sodium carbonate thereby formed is withdrawn at intervals through a retention tank when the temperature is maintained at 70-100 DEG C. thereby converting the solid anhydrous sodium carbonate to the desired monohydrate form. Water is added to maintain the solids concentration below 75% by weight and the slurry is preferably maintained in the tank until over 60% by weight of the monohydrate crystals have a size over 30 mesh. The monohydrate is separated in a centrifuge 30 and the solids passed through a dryer at 150 DEG C. where anhydrous sodium carbonate is formed. The mother liquor is recycled.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US882694XA | 1956-12-07 | 1956-12-07 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB882694A true GB882694A (en) | 1961-11-15 |
Family
ID=22210386
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB37969/57A Expired GB882694A (en) | 1956-12-07 | 1957-12-06 | Purification of sodium carbonate |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB882694A (en) |
-
1957
- 1957-12-06 GB GB37969/57A patent/GB882694A/en not_active Expired
Similar Documents
Publication | Publication Date | Title |
---|---|---|
ES8203323A1 (en) | Method of recovering in active form the catalyst for the terephthalic acid synthesis | |
GB962964A (en) | Dense sodium carbonate process | |
GB858844A (en) | Improvements in or relating to the production of alkali metal cyanides | |
US2764472A (en) | Brine purification | |
US2760992A (en) | Naphthalene | |
US2385483A (en) | Recovery and purification of iodine | |
GB1009260A (en) | Process for the preparation of dense soda ash | |
GB857385A (en) | Improvements in the preparation or persulphates | |
GB882694A (en) | Purification of sodium carbonate | |
GB964598A (en) | Production of soda ash | |
US2365417A (en) | Process of manufacturing sodium cyanide | |
US2863809A (en) | Process for concentration of caustic cell liquor | |
US2226576A (en) | Method of making sodium hyposulphite | |
US2812245A (en) | Sodium sulfide recovery | |
GB866039A (en) | Improvements in or relating to the recovery of germanium | |
GB443101A (en) | Improvements in and relating to the manufacture of sodium carbonate | |
US1992324A (en) | Manufacture of potassium carbonate and sodium sulphate | |
US2091309A (en) | Recovery of sulphuric acid in saccharification process | |
ES8305661A1 (en) | Process for obtaining molybdenum as a useful product from molybdeniferous solutions containing alkali metal carbonate, sulphate, hydroxide or hydrogen carbonate and possibly uranium | |
GB460281A (en) | Improvements in or relating to the production of potassium sulphate | |
US2045203A (en) | Decomposition of engel salt | |
SU129558A1 (en) | A method of processing carnallite mineral salts | |
GB911614A (en) | Improved process for salt purification | |
JPS5748949A (en) | Preparation of ethylenediaminetetraacetic acid alkali metal salt | |
GB428584A (en) | Improvements relating to processes for the treatment of lime aluminates |