GB1223233A - A process for production of calcium hypochlorite - Google Patents
A process for production of calcium hypochloriteInfo
- Publication number
- GB1223233A GB1223233A GB2564069A GB2564069A GB1223233A GB 1223233 A GB1223233 A GB 1223233A GB 2564069 A GB2564069 A GB 2564069A GB 2564069 A GB2564069 A GB 2564069A GB 1223233 A GB1223233 A GB 1223233A
- Authority
- GB
- United Kingdom
- Prior art keywords
- calcium hypochlorite
- sodium chloride
- chlorinating
- separating
- stage
- 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
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B11/00—Oxides or oxyacids of halogens; Salts thereof
- C01B11/04—Hypochlorous acid
- C01B11/06—Hypochlorites
- C01B11/064—Hypochlorites of alkaline-earth metals
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geology (AREA)
- Inorganic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
1,223,233. Calcium hypochlorite. NIPPON SODA CO. Ltd. 20 May, 1969, No. 25640/69. Heading C1A. Calcium hypochlorite is produced by chlorinating in a first stage a mixture of caustic soda and an aqueous solution saturated with sodium chloride and calcium hypochlorite, separating the precipitated sodium chloride, adding a calcium hydroxide-water slurry to the filtrate chlorinating in a second stage and separating the precipitated cyrstalline calcium hypochlorite and mother liquor from the reaction mixture. The mother liquor may be recycled as the aqueous saturated solution containing calcium hypochlorite and sodium chloride. Preferably, the caustic soda solution contains more than 50% by weight NaOH, and the reaction mixture should preferably always be at least just alkaline. The water content after the second chlorination should be between 58 and 68% by weight.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB2564069A GB1223233A (en) | 1969-05-20 | 1969-05-20 | A process for production of calcium hypochlorite |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB2564069A GB1223233A (en) | 1969-05-20 | 1969-05-20 | A process for production of calcium hypochlorite |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1223233A true GB1223233A (en) | 1971-02-24 |
Family
ID=10230950
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB2564069A Expired GB1223233A (en) | 1969-05-20 | 1969-05-20 | A process for production of calcium hypochlorite |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB1223233A (en) |
-
1969
- 1969-05-20 GB GB2564069A patent/GB1223233A/en not_active Expired
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