Method of separating fluor from gases of aluminium production
专利摘要:
Fluorine from waste gases is recovered by contacting the gases with aluminum oxide in the presence of steam. The steam increases the adsorption rate of the aluminum oxide thereby improving fluorine recovery. 公开号:SU728691A1 申请号:SU1896654 申请日:1973-03-21 公开日:1980-04-15 发明作者:Стейнеке Фредрик 申请人:Элкем-Спигерверкет А/С (Фирма); IPC主号:
专利说明:
This invention relates to methods for extracting fluorine from electrolytic melt aluminum production gases. The known method 11 is used to extract fluorine from waste gases of electrolytic furnaces of aluminum production, including their treatment with aluminum oxide in a fluidized bed apparatus followed by heat treatment of the sorbent separated from the gas stream by known methods. The method allows purification of fluorine gases by 98%. The disadvantages of this method are the loss of fluorine during the heat treatment of alumina and the low degree of extraction of fluorine. The aim of the invention is to increase the degree of fluorine recovery. The goal is achieved by the described method of separating fluorine from aluminum production gases, including contacting the gas with. alumina in a fluidized bed reactor in the presence of water vapor in the amount of 0.5-95% of the volume of the gas mixture at temperatures of 110. The essential difference of the proposed method is to carry out the process in the presence of water vapor, its content in the gas mixture, as well as the process temperature. This difference allows increasing the degree of defluorization to 99.9%. The data in the table confirm the optimality of the selected process parameters. From the data in the table it can be seen that fluorine adsorption increases with increasing percentage of vapor in the gas phase. An increase in the vapor content in the gas mixture above 95%, as well as an increase in temperature above 500 ° C, is impractical, since there is no further increase in fluorine recovery. A decrease in c: keeping the steam below 0.5% and a decrease in the process temperature below IIO-C leads to a decrease in the degree of fluorine release. Invention Formula The method of separating fluorine from aluminum production gases includes the 1st contacting of gas with aluminum oxide in a fluidized bed, characterized in that, for the purpose of increasing the degree of fluorine extraction, the process is 1TROWN in the presence of water vapor at a content of 0, 6% and a temperature in the gas mixture 110-500 ° C. Sources of information taken into account in the examination 1. The patent of France 2048338, cl. C 22 D 3/00 of 03/19/71 (prototype),
权利要求:
Claims (1) [1] Claim A method for separating fluorine from aluminum production gases, including contacting the gas with aluminum oxide in a fluidized bed, characterized in that, in order to • increase the degree of fluorine extraction, the process is carried out in the presence of water vapor when it is contained in a gas mixture of 0.5 ~ 95 vol. % and a temperature of 20 110-500 ° C.
类似技术:
公开号 | 公开日 | 专利标题 SU728691A1|1980-04-15|Method of separating fluor from gases of aluminium production JPH02120394A|1990-05-08|Method and apparatus for dehydration, deacidification, and separation of natural gas condensate SU587873A3|1978-01-05|Method of extracting mercury from gases GB1595674A|1981-08-12|Process for pressure stripping of sulphur dioxide from buffered solutions GB1021963A|1966-03-09|A process for working up waste gases containing hydrogen chloride JPS5717420A|1982-01-29|Recovering method for sodium thiocyanate JPS62443A|1987-01-06|Recovery of purifying solvent JPH01147026A|1989-06-08|Recovery of noble metal CA1107297A|1981-08-18|Recovery of acrylic acid from quench bottoms by addition of aluminum chloride ES422905A1|1976-05-01|Process for the extraction of mercury from gases JPS5778486A|1982-05-17|Preparation of meso-phase pitch SU893852A1|1981-12-30|Method of hydrogen chloride purification SU549420A1|1977-03-05|Phosphorus cleaning method SU740785A1|1980-06-15|Method of removing chloromethane from absorption gases of methylchlorosilane direct synthesis reactor SU551039A1|1977-03-25|Method of separating hydrogen fluoride from gas mixtures SU382719A1|1973-05-25|METHOD OF CLEANING MERCURY-CONTAINING GAS FROM MERCURY SU45922A1|1936-02-29|The method of regeneration of lime from sludge upon receipt of alumina from nepheline, etc. JPS62193626A|1987-08-25|Method for separating gaseous condensable component from gaseous mixture containing gaseous condensable component JPH01139124A|1989-05-31|Method for recovering and purifying ketone solvent SU130418A1|1959-11-30|Methods for extracting silicic acid from bauxite SU386838A1|1973-06-21|METHOD FOR PRODUCING CARBON DIOXIDE SU763260A1|1980-09-15|Method of phosphorus recovery from slime SU738378A1|1981-03-07|Method of primary treatment of coke gas SU508042A1|1981-03-15|Method of purifying titanium tetrachloride SU465904A1|1979-10-15|Method of extracting ethylene chloride
同族专利:
公开号 | 公开日 CS189591B2|1979-04-30| HU165523B|1974-09-28| FR2176817A1|1973-11-02| SE436736B|1985-01-21| YU39270B|1984-10-31| BE797066A|1973-07-16| DE2313495A1|1973-10-04| ES412890A1|1975-12-16| CA982786A|1976-02-03| BR7302019D0|1974-07-25| NL7303509A|1973-09-25| FR2176817B1|1976-04-09| NO131825B|1975-05-05| NL154989B|1977-11-15| ZA731280B|1974-10-30| YU59573A|1982-06-30| NO131825C|1975-08-13| DE2313495C2|1982-10-07| OA04670A|1980-12-31| CH588417A5|1977-05-31| JPS5792B2|1982-01-05| AT322867B|1975-06-10| IT979616B|1974-09-30| US3813852A|1974-06-04| GB1389769A|1975-04-09| JPS497191A|1974-01-22| AU5356173A|1974-09-26| SU728691A3|1980-04-15|
引用文献:
公开号 | 申请日 | 公开日 | 申请人 | 专利标题 CA613352A|1961-01-24|Aluminum Company Of America|Electrolytic production of aluminum| US2059553A|1933-10-02|1936-11-03|Harry V Churchill|Removal of fluorine from water| US3503184A|1968-03-07|1970-03-31|Aluminum Co Of America|Treatment of gases evolved in the production of aluminum| US3721066A|1970-12-29|1973-03-20|Teller Environmental Systems|Process for recovery of acid gases| US3760565A|1971-07-19|1973-09-25|Aluminum Co Of America|Anti-pollution method|JPS5269284U|1976-08-17|1977-05-23| US4415317A|1981-02-09|1983-11-15|The Trane Company|Wrap element and tip seal for use in fluid apparatus of the scroll type| JPS61132494U|1985-02-07|1986-08-19| JPS62284981A|1986-06-02|1987-12-10|Matsushita Refrig Co|Scroll compressor| JPH02114785U|1989-03-01|1990-09-13| US5160512A|1992-01-13|1992-11-03|Cleveland State University|Gas separation process| US6905663B1|2000-04-18|2005-06-14|Jose I. Arno|Apparatus and process for the abatement of semiconductor manufacturing effluents containing fluorine gas| US6514471B1|2000-10-31|2003-02-04|Air Products And Chemicals, Inc.|Removing fluorine from semiconductor processing exhaust gas| GB0101769D0|2001-01-24|2001-03-07|Ineos Fluor Ltd|Decomposition of fluorine compounds| US7569193B2|2003-12-19|2009-08-04|Applied Materials, Inc.|Apparatus and method for controlled combustion of gaseous pollutants| US7736599B2|2004-11-12|2010-06-15|Applied Materials, Inc.|Reactor design to reduce particle deposition during process abatement| JP5102217B2|2005-10-31|2012-12-19|アプライドマテリアルズインコーポレイテッド|Process reduction reactor| JP6090845B2|2013-03-06|2017-03-08|国立研究開発法人農業・食品産業技術総合研究機構|Suction type seed selection device| CN104911631A|2015-06-18|2015-09-16|中国科学院过程工程研究所|Novel method for efficiently purifying aluminum electrolysis fluorine-containing flue gas by using porous alumina|
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申请号 | 申请日 | 专利标题 NO943/72A|NO131825C|1972-03-22|1972-03-22| 相关专利
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