GB396256A - Process of and apparatus for the production of bleaching powder - Google Patents
Process of and apparatus for the production of bleaching powderInfo
- Publication number
- GB396256A GB396256A GB30879/32A GB3087932A GB396256A GB 396256 A GB396256 A GB 396256A GB 30879/32 A GB30879/32 A GB 30879/32A GB 3087932 A GB3087932 A GB 3087932A GB 396256 A GB396256 A GB 396256A
- Authority
- GB
- United Kingdom
- Prior art keywords
- chlorine
- water
- stage
- air
- reduced pressure
- 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
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
- Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geology (AREA)
- Inorganic Chemistry (AREA)
- Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
Abstract
Bleaching-powder of low water-content is obtained in an intermittent process by the action of chlorine on lime by first chlorinating under such conditions that no substantial quantity of water is removed and until a moderate chlorine concentration at which the "wet point" is not reached is attained, and then, chlorination being continued, gradually removing water in such measure that the granular character is preserved without impairing the capacity for absorbing chlorine. In the first stage, the temperature is maintained below 40 DEG C., preferably between 25-35 DEG C. In examples, the chlorine concentration of the product of this stage varies from 23-32 per cent. In the second stage, water is removed by the use of a temperature above 45 DEG C., and preferably between 50 - 55 DEG C., with or without reduced pressure. As an alternative to reduced pressure, the water may be carried off by air employed to dilute the chlorine, or if concentrated chlorine is used, a special current of air may be passed through the apparatus. The dilute chlorine or air may be preheated to 35 DEG C. Near the end of the chlorination, the air current is decreased or shut off. When the product contains at least 36 per cent chlorine, it is completely dehydrated as by treatment with air at 45-55 DEG C. In a modification in which a pulverulent product is obtained, a continuous removal of a moderate amount of water in the first stage may be effected under a reduced pressure decreasing from 90-40 mms. mercury, a pressure of 30-50 mms. being maintained in the second stage. A suitable apparatus consists of a water-jacketed iron drum, provided with an axially mounted shaft carrying paddles, the ends of which are provided with spring-pressed scrapers. Chlorine inlets are distributed over the upper side of the shell.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE396256X | 1931-11-02 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB396256A true GB396256A (en) | 1933-08-03 |
Family
ID=6396990
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB30879/32A Expired GB396256A (en) | 1931-11-02 | 1932-11-02 | Process of and apparatus for the production of bleaching powder |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB396256A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113321187A (en) * | 2021-05-24 | 2021-08-31 | 中国成达工程有限公司 | Method and system for producing bleaching powder by using wet-process acetylene waste calcium carbide slurry |
-
1932
- 1932-11-02 GB GB30879/32A patent/GB396256A/en not_active Expired
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113321187A (en) * | 2021-05-24 | 2021-08-31 | 中国成达工程有限公司 | Method and system for producing bleaching powder by using wet-process acetylene waste calcium carbide slurry |
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