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 carriers

Info

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
Application number
GB26582/51A
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.)
GEA Group AG
Original Assignee
Metallgesellschaft 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 Metallgesellschaft AG filed Critical Metallgesellschaft AG
Publication of GB704810A publication Critical patent/GB704810A/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
    • C01B32/00Carbon; Compounds thereof
    • C01B32/30Active carbon
    • C01B32/312Preparation
    • C01B32/336Preparation 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.
GB26582/51A 1950-11-29 1951-11-13 Improvements in or relating to the production of activated carbon, catalysts or catalyst carriers Expired GB704810A (en)

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)

* Cited by examiner, † Cited by third party
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

Cited By (8)

* Cited by examiner, † Cited by third party
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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