GB565089A - Improvements in production of neutral calcium hypochlorite - Google Patents

Improvements in production of neutral calcium hypochlorite

Info

Publication number
GB565089A
GB565089A GB1328/43A GB132843A GB565089A GB 565089 A GB565089 A GB 565089A GB 1328/43 A GB1328/43 A GB 1328/43A GB 132843 A GB132843 A GB 132843A GB 565089 A GB565089 A GB 565089A
Authority
GB
United Kingdom
Prior art keywords
slurry
dibasic
per cent
lime
gravity
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
GB1328/43A
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.)
Mathieson Alkali Works Inc
Original Assignee
Mathieson Alkali Works Inc
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 Mathieson Alkali Works Inc filed Critical Mathieson Alkali Works Inc
Publication of GB565089A publication Critical patent/GB565089A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B11/00Oxides or oxyacids of halogens; Salts thereof
    • C01B11/04Hypochlorous acid
    • C01B11/06Hypochlorites
    • C01B11/064Hypochlorites of alkaline-earth metals

Abstract

565,089. Calcium hypochlorite. MATHIESON ALKALI WORKS. Jan. 26, 1943, No. 1328. Convention date, Jan. 21, 1942. [Class 1 (iii)] Easily filtered slurries of neutral calcium hypochlorite are produced by simultaneously adding to a previously prepared slurry thereof, at rates which are substantially equivalent chemically, chlorine and a slurry of dibasic calcium hypochlorite, the liquid phase of the latter having a gravity of 30-47, preferably 40-44‹ Tw. The free lime content of the composite slurry is generally kept below 1.5 per cent by weight during the chlorination which is effected at 10-25, preferably 15-20‹ C. The dibasic slurry may be added continuously or intermittently to a neutral slurry, prepared initially by chlorination of lime or the dibasic compound until the free lime content is below 1.5, usually about 0.5 per cent by weight. The dibasic slurry may be prepared by chlorinating milk of lime, starting at room temperature and rising to 35-45‹ C. until substantially complete conversion when, if desired, part of the mother liquor may be drawn off after settling, and further chlorine added until the liquid phase has the desired gravity. The dibasic compound may be separated and resuspended. In a batch operation, when the reaction chamber is full, the addition of dibasic slurry is stopped, further chlorination to a lime content of 0.1-0.2 per cent effected if desired, and the neutral slurry removed leaving sufficient for the next operation. In continuous operation, four tanks may be used, milk of lime being chlorinated in the first at 30-40‹ C. to a gravity of 22-26‹ Tw., and further chlorinated in the next at 35-40‹ C. to a gravity of 40-47‹ Tw. The slurry is passed to the third tank containing the neutral slurry, while chlorine is introduced to keep the free lime content below 1.5 per cent, the product being finally reduced in lime content to, say, .05-.25 per cent by chlorine in the last tank, which may be cooled to, say, 0‹ C. Examples of batch and continuous operation are given.
GB1328/43A 1942-01-21 1943-01-26 Improvements in production of neutral calcium hypochlorite Expired GB565089A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US565089XA 1942-01-21 1942-01-21

Publications (1)

Publication Number Publication Date
GB565089A true GB565089A (en) 1944-10-26

Family

ID=22004865

Family Applications (1)

Application Number Title Priority Date Filing Date
GB1328/43A Expired GB565089A (en) 1942-01-21 1943-01-26 Improvements in production of neutral calcium hypochlorite

Country Status (1)

Country Link
GB (1) GB565089A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2457838A1 (en) * 1979-05-29 1980-12-26 Toyo Soda Mfg Co Ltd STABLE CALCIUM HYPOCHLORITE COMPOSITION AND PREPARATION THEREOF
FR2584384A1 (en) * 1985-07-05 1987-01-09 Atochem DISCONTINUED PROCESS FOR THE TWO-CHLORINATION PREPARATION OF HYDRATED CALCIUM HYDROCHLORITE HYDROCHLORITE

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2457838A1 (en) * 1979-05-29 1980-12-26 Toyo Soda Mfg Co Ltd STABLE CALCIUM HYPOCHLORITE COMPOSITION AND PREPARATION THEREOF
FR2584384A1 (en) * 1985-07-05 1987-01-09 Atochem DISCONTINUED PROCESS FOR THE TWO-CHLORINATION PREPARATION OF HYDRATED CALCIUM HYDROCHLORITE HYDROCHLORITE
EP0213003A1 (en) * 1985-07-05 1987-03-04 Elf Atochem S.A. Discontinuous two-stage chlorination process for the production of neutral hydrated calcium hypochlorite

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