GB386208A - Process for the production of potassium carbonate - Google Patents
Process for the production of potassium carbonateInfo
- Publication number
- GB386208A GB386208A GB1509332A GB1509332A GB386208A GB 386208 A GB386208 A GB 386208A GB 1509332 A GB1509332 A GB 1509332A GB 1509332 A GB1509332 A GB 1509332A GB 386208 A GB386208 A GB 386208A
- Authority
- GB
- United Kingdom
- Prior art keywords
- potassium
- solution
- carbonate
- bicarbonate
- sulphate
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Inorganic Chemistry (AREA)
- Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
Abstract
Potassium carbonate is obtained by reacting an aqueous solution or suspension of potassium sulphate and alkaline-earth hydroxides with carbon monoxide or gases containing it and converting the resulting potassium formate into carbonate by calcination. The potassium formate solution resulting from the first step, after the separation of precipitated alkalineearth sulphate, is preferably treated with excess of potassium carbonate or bicarbonate to precipitate impurities, the purified solution containing formate and carbonate being evaporated to dryness for calcination ; or only sufficient potassium carbonate or bicarbonate to precipitate the impurities may be added to the solution, a further quantity of carbonate or bicarbonate being added to the dry product after evaporation. According to one example, an aqueous suspension of potassium sulphate and quick lime is treated with purified producer gas in an iron stirrer-autoclave at 200 DEG C. and 15 atmospheres pressure. The resulting solution is filtered from gypsum, evaporated to dryness and calcined. According to a second example, the potassium formate solution, prepared as in the foregoing example, after the separation of gypsum is heated and potassium carbonate or bicarbonate is added. Ferric oxide, alumina and calcium carbonate precipitate and the remaining solution is concentrated, whereupon unconverted potassium sulphate precipitates, is separated and returned to the process. The purified solution is dehydrated mixed with ground potassium carbonate and calcined.ALSO:Potassium carbonate is obtained by reacting an aqueous solution or suspension of potassium sulphate and alkaline-earth hydroxides with carbon monoxide or gases containing it and converting the resulting potassium formate into carbonate by calcination. The potassium formate solution resulting from the first step, after the separation of precipitated alkaline-earth sulphate, is preferably treated with excess of potassium carbonate or bicarbonate to precipitate impurities, the purified solution containing formate and carbonate being evaporated to dryness for calcination; or only sufficient potassium carbonate or bicarbonate to precipitate the impurities may be added to the solution, a further quantity of carbonate or bicarbonate being added to the dry product after evaporation. The calcination may be carried out in a continuous process in a rotary furnace with the gases of combustion in parallel flow. According to one example an aqueous suspension of potassium sulphate and quick lime is treated with purified producer gas in an iron stirrer-autoclave at 200 DEG C. and 15 atmospheres pressure. The resulting solution is filtered from gypsum, evaporated to dryness and calcined. According to a second example, the potassium formate solution, prepared as in the foregoing example, after the separation of gypsum is heated and potassium carbonate or bicarbonate is added. Ferric oxide, alumina and calcium carbonate precipitate and the remaining solution is concentrated, whereupon unconverted potassium sulphate precipitates, is separated and returned to the process. The purified solution is dehydrated, mixed with ground potassium carbonate and calcined.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB1509332A GB386208A (en) | 1932-05-27 | 1932-05-27 | Process for the production of potassium carbonate |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB1509332A GB386208A (en) | 1932-05-27 | 1932-05-27 | Process for the production of potassium carbonate |
Publications (1)
Publication Number | Publication Date |
---|---|
GB386208A true GB386208A (en) | 1933-01-12 |
Family
ID=10052896
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB1509332A Expired GB386208A (en) | 1932-05-27 | 1932-05-27 | Process for the production of potassium carbonate |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB386208A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2590412A (en) * | 1947-11-14 | 1952-03-25 | Zuid Nl Spiritusfabriek Nv | Method of working up the waste liquor of fermentation industries in which molasses are used |
US5057294A (en) * | 1989-10-13 | 1991-10-15 | The University Of Tennessee Research Corporation | Recovery and regeneration of spent MHD seed material by the formate process |
-
1932
- 1932-05-27 GB GB1509332A patent/GB386208A/en not_active Expired
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2590412A (en) * | 1947-11-14 | 1952-03-25 | Zuid Nl Spiritusfabriek Nv | Method of working up the waste liquor of fermentation industries in which molasses are used |
US5057294A (en) * | 1989-10-13 | 1991-10-15 | The University Of Tennessee Research Corporation | Recovery and regeneration of spent MHD seed material by the formate process |
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