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GB668612A - Method of producing coarsely crystalline sodium carbonate monohydrate - Google Patents

Method of producing coarsely crystalline sodium carbonate monohydrate

Info

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
Application number
GB19830/50A
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.)
Kali Chemie AG
Original Assignee
Kali Chemie AG
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 Kali Chemie AG filed Critical Kali Chemie AG
Publication of GB668612A publication Critical patent/GB668612A/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
    • C01D7/35Varying 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.
GB19830/50A 1949-08-16 1950-08-09 Method of producing coarsely crystalline sodium carbonate monohydrate Expired GB668612A (en)

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)

* Cited by examiner, † Cited by third party
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

Cited By (4)

* Cited by examiner, † Cited by third party
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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