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    • 1. 发明授权
    • Recovery of fluorine from waste gases
    • 从废气中回收氟
    • US4613494A
    • 1986-09-23
    • US689787
    • 1985-01-08
    • James C. Barber
    • James C. Barber
    • C01B9/08C01B33/18C05B7/00C01D3/02C01B33/12C01D1/16C01D11/02
    • C01B33/186C01B9/08C05B7/00C01P2002/02C01P2006/80
    • Fluorine in phosphate ores is present as the mineral fluorapatite. When the ores are digested with sulfuric acid a slurry is formed which can be filtered to make wet-process phosphoric acid. But fluorine compounds are discharged into the surrounding air during digestion and filtration. The fluorine-containing air is scrubbed with water to prevent air pollution. Scrubber water is cooled in ponds and is recycled to the scrubber. However, fluorine compounds are emitted from the cooling ponds and cause air pollution. In the present invention, processes are disclosed for treating fluorine-containing gases without use of cooling ponds thereby eliminating the air pollution problem. A facility is provided for treating fluorine-containing gases wherein fluosilicic acid or fluosilicate salts are converted to a fluoride salt by the addition of an alkaline substance. A slightly acidic scrubber water is concentrated in an absorption tower. When the scrubber water contains nutrients, ammonium is the preferred alkaline substance and the scrubber water is recovered in solid ammonium phosphate fertilizers or in suspension fertilizers. Sodium hydroxide or sodium carbonate are the perferred alkaline substances when sodium cryolite or aluminum fluoride are produced.
    • 作为矿物氟磷灰石存在磷酸盐矿中的氟。 当矿石用硫酸消化时,形成可以过滤以制备湿法磷酸的浆料。 但氟化合物在消化和过滤期间排放到周围的空气中。 含氟空气用水擦洗以防止空气污染。 洗涤水在池塘中冷却并被再循环到洗涤器中。 然而,氟化合物从冷却池排出并引起空气污染。 在本发明中,公开了用于处理含氟气体而不使用冷却池的方法,从而消除了空气污染问题。 提供一种用于处理含氟气体的设备,其中通过加入碱性物质将氟硅酸或氟硅酸盐转化为氟化物盐。 稍微酸性的洗涤器水浓缩在吸收塔中。 当洗涤器水含有营养物质时,铵是优选的碱性物质,洗涤器水在固体磷酸铵肥料或悬浮肥料中回收。 氢氧化钠或碳酸钠是生产钠冰晶石或氟化铝时的优先使用的碱性物质。
    • 3. 发明授权
    • Recovery of lithium carbonate
    • 回收碳酸锂
    • US3857920A
    • 1974-12-31
    • US16733771
    • 1971-07-29
    • DEPARTMENT OF HEALTH EDUCATION
    • GRANTHAM LYOSIM S
    • C01D15/08C22B26/12C01D11/02C01D7/22
    • C22B26/12C01D15/08Y10S423/12
    • Lithium carbonate is recovered from an aqueous slurry by first treating the sparingly soluble lithium carbonate with carbon dioxide to convert it to the much more soluble lithium bicarbonate. The bicarbonate solution is next separated from insoluble material present and then decarbonated to precipitate lithium carbonate, which is then recovered. The present process is of particular utility for the recovery of lithium carbonate from fly ash- and coke-containing filter cakes resulting from a process for the treatment of flue gas to remove sulfur dioxide present therein by absorption of the sulfur dioxide in a molten alkali metal carbonate mixture.
    • 通过首先用二氧化碳处理微溶碳酸锂以将其转化为更易溶解的碳酸氢锂,从含水浆液中回收碳酸锂。 然后将碳酸氢盐溶液与存在的不溶物分离,然后脱碳以沉淀碳酸锂,然后回收碳酸锂。 本发明的方法特别适用于从通过吸收二氧化硫在熔融碱金属中处理烟道气以除去二氧化硫的方法得到的粉煤灰和含焦炭滤饼中回收碳酸锂 碳酸盐混合物。
    • 8. 发明授权
    • Process for the production of lithium chloride
    • 氯化锂生产工艺
    • US3872220A
    • 1975-03-18
    • US43619574
    • 1974-01-24
    • FOOTE MINERAL CO
    • SMITH JR WILLIAM NOVIS
    • C01D15/04C01D11/02
    • C01D15/04
    • This invention relates to a process for the production of lithium chloride substantially free of lithium salts of chlorine oxygen acids through substantially quantitative conversion of chlorine in a gas stream to lithium chloride. Chlorine in a gas stream is absorbed in a substantially saturated solution of lithium hydroxide until the lithium hydroxide is converted to a solution of lithium chloride containing lithium salts of chlorine oxygen acids. The latter solution is then treated with ammonia to convert lithium hypochlorite and lithium chlorite present therein to lithium chloride followed by acidification of the solution and treatment with an organic reducing agent to convert lithium chlorate and lithium perchlorate therein to lithium chloride.
    • 本发明涉及通过将气流中的氯基本上定量地转化为氯化锂,生产基本上不含氯氧酸的锂盐的氯化锂的方法。 将气流中的氯吸收在基本上饱和的氢氧化锂溶液中,直到氢氧化锂转化为含有氯氧酸的锂盐的氯化锂溶液。 然后用氨处理后者溶液以将其中存在的次氯酸锂和亚氯酸锂转化为氯化锂,然后酸化溶液并用有机还原剂处理以将氯酸锂和其中的高氯酸锂转化为氯化锂。
    • 9. 发明授权
    • Method of preparing purified lithium aluminum chloride
    • 制备纯化的氯化锂铝的方法
    • US3761578A
    • 1973-09-25
    • US3761578D
    • 1972-03-09
    • ANDERSON S
    • ANDERSON S
    • C01F7/00C01D11/02C01F7/56
    • C01F7/002
    • Purified lithium aluminum chloride (LiAlCl4) is prepared by passing hydrogen chloride gas through a melt of lithium aluminum chloride containing impurities such as water, hydroxides or other inorganic oxygen-containing salts, carbon and iron, to remove at least a portion of the water and oxygen-containing impurities. Thereafter, the melt is heated to a temperature of from about 425* to about 540* C. and chlorine gas is passed through the melt to remove carbon impurities. The melt is cooled to about 190* C. to 260* C. and contacted with aluminum to replace the iron in solution because of its higher electrochemical potential. The purified melt is filtered and cooled. Analysis of a typical product shows less than 300 parts per billion of impurities. The starting lithium aluminum chloride may advantageously be prepared by melting admixture of reagent grade lithium chloride and reagent grade aluminum chloride. Mixture of lithium aluminum chloride and aluminum chloride can be prepared using an excess of reagent grade aluminum chloride reactant.
    • 通过使氯化氢气体通过含有诸如水,氢氧化物或其它无机含氧盐(碳和铁)的杂质的氯化锂的熔体,以除去至少一部分水和/或其中的至少一部分来制备纯化的氯化锂铝(LiAlCl 4) 含氧杂质。 此后,将熔体加热至约425℃至约540℃的温度,并将氯气通过熔体以除去碳杂质。 将熔体冷却至约190℃至260℃,并与铝接触以替代溶液中的铁,因为它具有较高的电化学势。 将纯化的熔体过滤并冷却。 典型产品的分析显示不到百亿分之十十分之杂质。 起始的氯化锂铝可以有利地通过将试剂级氯化锂和试剂级氯化铝混合来制备。 可以使用过量的试剂级氯化铝反应物制备氯化锂铝和氯化铝的混合物。