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    • 5. 发明授权
    • Method of producing crystalline ammonium metatungstate
    • 生产结晶态偏钨酸铵的方法
    • US4612182A
    • 1986-09-16
    • US704843
    • 1985-02-25
    • Tai K. KimMartin B. MacInnisRobert P. McClintic
    • Tai K. KimMartin B. MacInnisRobert P. McClintic
    • C01G41/00
    • C01G41/00
    • A method is disclosed for producing crystalline ammonium metatungstate from ammonium paratungstate. The method involves heating the ammonium paratungstate at from about 100.degree. C. to about 250.degree. C. for from about 1 hour to about 8 hours to remove some ammonia and water, digesting a solution of the heated ammonium paratungstate in water at from about 80.degree. C. to about 100.degree. C. for from about 2 hours to about 6 hours at relatively constant volume while maintaining the pH of the slurry at from about 4.2 to about 3.0 by addition of ammonia as necessary to form a solution of ammonium metatungstate in water. The ammonium metatungstate solution is then evaporated to concentrate it. Any insoluble material is separated from the solution. Ammonium metatungstate is then crystallized from the resulting concentrated ammonium metatungstate solution.
    • 公开了一种从仲钨酸铵生产结晶态偏钨酸铵的方法。 该方法包括将约100℃至约250℃的仲钨酸铵加热约1小时至约8小时以除去一些氨和水,在约80℃的水中将加热的仲钨酸铵溶液消化 以相对恒定的体积进行约2小时至约6小时,同时通过根据需要加入氨将浆料的pH保持在约4.2至约3.0,以形成偏钨酸铵溶液 水。 然后将偏钨酸铵溶液蒸发浓缩。 将任何不溶物质与溶液分离。 然后从所得浓缩的偏钨酸铵溶液中结晶偏钨酸铵。
    • 9. 发明授权
    • Separating molybdenum values from an aqueous solution containing
tungsten by solvent extraction
    • 通过溶剂萃取从含钨的水溶液中分离钼值
    • US4288413A
    • 1981-09-08
    • US158967
    • 1980-06-12
    • Martin B. MacInnisTai K. Kim
    • Martin B. MacInnisTai K. Kim
    • C01G39/00C01G41/00C22B3/28
    • C22B3/0016C01G39/003C01G41/006Y02P10/234Y10S423/14
    • The process is described wherein molybdenum values are separated from an aqueous solution containing tungsten. The molybdenum is converted to a thiomolybdate ion and the resulting solution is contacted with a suitable amount of organic extractant for a sufficient period of time to preferentially extract the thiomolybdate. The organic extractant including the thiomolybdate is separated from the aqueous solution comprising the unextracted tungsten values. The molybdenum values are stripped from the separated organic extractant by contacting with an aqueous solution containing sufficient amount of an oxidizing agent suitable for oxidizing the thiomolybdate complex ion to the molybdate ion which in turn is soluble in the aqueous solution. The organic extractant is then recycled for extracting the thiomolybdate complex ion and the molybdate ion may be recovered from the aqueous solution by conventional methods.
    • 描述了其中钼值与含钨水溶液分离的方法。 将钼转化成硫钼酸根离子,使所得溶液与适量的有机萃取剂接触足够的时间以优先提取硫钼酸盐。 包括硫钼酸盐的有机萃取剂与包含未萃取的钨值的水溶液分离。 通过与含有足够氧化硫钼酸盐配合物的氧化剂的水溶液与钼酸根离子接触而将钼值从分离的有机萃取剂中剥离,钼酸根离子又溶于水溶液中。 然后将有机萃取剂再循环用于提取硫钼酸盐络合物离子,并且可以通过常规方法从水溶液中回收钼酸根离子。
    • 10. 发明授权
    • Method of producing crystalline ammonium metatungstate
    • 生产结晶态偏钨酸铵的方法
    • US4612183A
    • 1986-09-16
    • US704992
    • 1985-02-25
    • Tai K. KimCarl W. BoyerMartin B. MacInnisDonald H. Ennis
    • Tai K. KimCarl W. BoyerMartin B. MacInnisDonald H. Ennis
    • C01G41/00
    • C01G41/00
    • A method is disclosed for producing crystalline ammonium metatungstate from ammonium paratungstate. The method involves heating ammonium paratungstate in a multiple hearth furnace at from about 200.degree. C. to about 400.degree. C. to form a relatively uniformly heated ammonium paratungstate. A slurry of the heated ammonium paratungstate in water is then digested at from about 70.degree. C. to about 100.degree. C. for less than about 6 hours at relatively constant volume while maintaining the pH of the slurry at from about 4.2 to about 3.0 by the addition of ammonia as necessary to form a solution of ammonium metatungstate. The resulting ammonium metatungstate solution is then evaporated to a fraction of its original volume to concentrate it and any insolubles are removed. The ammonium metatungstate is then crystallized from the concentrated solution.
    • 公开了一种从仲钨酸铵生产结晶态偏钨酸铵的方法。 该方法包括在约200℃至约400℃的多床炉中加热仲钨酸铵,形成相对均匀加热的仲钨酸铵。 然后将加热的仲钨酸铵的浆液在约70℃至约100℃下以相对恒定的体积消化少于约6小时,同时通过以下方式将浆料的pH维持在约4.2至约3.0,通过 根据需要添加氨以形成偏钨酸铵溶液。 然后将所得的偏钨酸铵溶液蒸发至其原始体积的一部分以使其浓缩并除去任何不溶物。 然后从浓缩溶液中结晶偏钨酸铵。