GB704810A - Improvements in or relating to the production of activated carbon, catalysts or catalyst carriers - Google Patents
Improvements in or relating to the production of activated carbon, catalysts or catalyst carriersInfo
- Publication number
- GB704810A GB704810A GB26582/51A GB2658251A GB704810A GB 704810 A GB704810 A GB 704810A GB 26582/51 A GB26582/51 A GB 26582/51A GB 2658251 A GB2658251 A GB 2658251A GB 704810 A GB704810 A GB 704810A
- Authority
- GB
- United Kingdom
- Prior art keywords
- activated
- heat
- activating
- activation
- gas
- 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
- C01B32/00—Carbon; Compounds thereof
- C01B32/30—Active carbon
- C01B32/312—Preparation
- C01B32/336—Preparation characterised by gaseous activating agents
Abstract
In producing materials with surface active properties, especially activated carbon, catalysts, or catalyst carriers, from carbonaceous substances, such as wood, peat, coke, brown or mineral coal, which are conducted through the activating zone by means of an activating or inert gas, the requisite heat for activation is partly or wholly transmitted to a mixture of the substances to be activated and the gaseous activating agents and/or other activating agents by means of moving heat transferring solids and the heat transferring solids are subsequently separated from the activated product, e.g. by difference in specific gravity. The heat carriers, which may be reheated and reused after giving up utilisable heat, may be ceramic substances, e.g. alumina or other metal oxides, quartz, refractory silicates, metals, silicon, silicon carbide, or carbonaceous substances, e.g. coke, coal, or graphite, preferably of specific heat exceeding 0.3, moving countercurrent, cocurrent, or transverse current, or any combination of these, to the gas carrying the material to be activated. Heat remaining in the heat carrier may be used for preheating. If a carbonaceous heat carrier is used part may become activated and may be separated from the non-activated part, which is reused. The heat carrier may be heated outside the treatment zone by fuel combustion, or, if combustible materials are used as heat carriers, these may be heated by partial combustion outside the treatment chamber. Heat may also be supplied by fuel combustion during the activation and the gases generated in the activation may be used for this purpose. The material to be activated, which may be pre-dried, may be carried in suspension in activating gases, e.g. carbon dioxide or steam, or may form a fluidized bed with the heat carrier passing therethrough, and part or all of the activated carbon may be treated more than once. The material to be activated may be impregnated with chemical activating agents, e.g. alkali metal hydroxides or salts, zinc chloride, or phosphoric or sulphuric acids, and by use of inert gas or activating gas at 200-500 DEG C., or activating gas at 500-600 DEG C. or above chemical activation alone or a combination of chemical and gas activation may be effected. The activated product may be separated in cyclones, with or without a simultaneous division into fractions on grain size by screening, on ash content, or on specific gravity or bulk density by elutriation, or the division into fractions may be effected after separation. The activated product or the fractions may be after treated with distilled water, acids, alkalies, or solution of salts of alkali, alkaline earth or heavy metals, or with impregnating chemicals for specified purposes, e.g. iodine, alkalies, copper salts, phosphoric acid, wetting agents, or fats or oils. The activated product may be partly or wholly ground, agglomerated with a binder with or without impregnating chemicals and subjected to further activation, or classified by electrostatic precipitation. Specifications 676,391 and 679,095 are referred to.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE704810X | 1950-11-29 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB704810A true GB704810A (en) | 1954-03-03 |
Family
ID=6616708
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB26582/51A Expired GB704810A (en) | 1950-11-29 | 1951-11-13 | Improvements in or relating to the production of activated carbon, catalysts or catalyst carriers |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB704810A (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE2242411A1 (en) * | 1971-09-04 | 1973-04-12 | Takeda Chemical Industries Ltd | MANUFACTURING METHOD FOR COARSE ACTIVATED CARBON PARTICLES |
EP0076457A2 (en) * | 1981-10-01 | 1983-04-13 | Bergwerksverband GmbH | Process and apparatus for the regeneration of moist, powdery adsorbents |
GB2121018A (en) * | 1982-06-02 | 1983-12-14 | Anthony Constantine | Method of and apparatus for the production of charcoal |
DE3222153A1 (en) * | 1982-06-12 | 1983-12-15 | Bayer Ag, 5090 Leverkusen | Process for carrying out gas-solid reactions in a fluidised bed |
US4476789A (en) * | 1982-05-31 | 1984-10-16 | Anthony Constantine | Method of and apparatus for the production of charcoal |
NO341618B1 (en) * | 2004-12-27 | 2017-12-11 | Svenska Aerogel Ab | Agglomerates of precipitated silica, process for preparing it as filter medium by gas filtration |
-
1951
- 1951-11-13 GB GB26582/51A patent/GB704810A/en not_active Expired
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE2242411A1 (en) * | 1971-09-04 | 1973-04-12 | Takeda Chemical Industries Ltd | MANUFACTURING METHOD FOR COARSE ACTIVATED CARBON PARTICLES |
US3852216A (en) * | 1971-09-04 | 1974-12-03 | Takeda Chemical Industries Ltd | Process for producing coarse particles of active carbon in a fluidized bed with added inert particles |
EP0076457A2 (en) * | 1981-10-01 | 1983-04-13 | Bergwerksverband GmbH | Process and apparatus for the regeneration of moist, powdery adsorbents |
EP0076457A3 (en) * | 1981-10-01 | 1984-01-11 | Bergwerksverband Gmbh | Process and apparatus for the regeneration of moist, powdery adsorbents |
US4476789A (en) * | 1982-05-31 | 1984-10-16 | Anthony Constantine | Method of and apparatus for the production of charcoal |
GB2121018A (en) * | 1982-06-02 | 1983-12-14 | Anthony Constantine | Method of and apparatus for the production of charcoal |
DE3222153A1 (en) * | 1982-06-12 | 1983-12-15 | Bayer Ag, 5090 Leverkusen | Process for carrying out gas-solid reactions in a fluidised bed |
NO341618B1 (en) * | 2004-12-27 | 2017-12-11 | Svenska Aerogel Ab | Agglomerates of precipitated silica, process for preparing it as filter medium by gas filtration |
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