GB386208A - Process for the production of potassium carbonate - Google Patents

Process for the production of potassium carbonate

Info

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
Application number
GB1509332A
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
CHEM FAB BUCKAU
Original Assignee
CHEM FAB BUCKAU
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by CHEM FAB BUCKAU filed Critical CHEM FAB BUCKAU
Priority to GB1509332A priority Critical patent/GB386208A/en
Publication of GB386208A publication Critical patent/GB386208A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01DCOMPOUNDS OF ALKALI METALS, i.e. LITHIUM, SODIUM, POTASSIUM, RUBIDIUM, CAESIUM, OR FRANCIUM
    • C01D7/00Carbonates 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.
GB1509332A 1932-05-27 1932-05-27 Process for the production of potassium carbonate Expired GB386208A (en)

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)

* Cited by examiner, † Cited by third party
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

Cited By (2)

* Cited by examiner, † Cited by third party
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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