会员体验
专利管家(专利管理)
工作空间(专利管理)
风险监控(情报监控)
数据分析(专利分析)
侵权分析(诉讼无效)
联系我们
交流群
官方交流:
QQ群: 891211   
微信请扫码    >>>
现在联系顾问~
热词
    • 2. 发明授权
    • Process for recovering tungsten from tungsten bearing material
containing arsenic
    • 从含砷的钨轴承材料中回收钨的工艺
    • US4741886A
    • 1988-05-03
    • US922651
    • 1986-10-24
    • Clarence D. VanderpoolRichard A. ScheithauerMartin B. MacInnis
    • Clarence D. VanderpoolRichard A. ScheithauerMartin B. MacInnis
    • C01G41/00
    • C01G41/00
    • A process is disclosed for recovering tungsten from tungsten bearing material containing arsenic. The process involves adjusting a water slurry of the material to a pH of less than about 4 with an acid to solubilize the major portion of the tungsten, adding an insoluble ferric compound to the slurry to form a two phase system in which the solid phase contains the major portion of the arsenic and of any phosphorus which may be present, and a solution phase containing the major portion of the tungsten. After separation of the solid from the solution, the solution is adjusted to a pH of less than about 2 with an acid and a suffficient amount of hexamethylenetetramine is added to the solution to precipitate the major portion of the tungsten, followed by separating the precipitate from the resulting liquor. The solid phase containing the arsenic and phosphorus, if any, can be contacted with water and a soluble ferric salt to produce a treated solid which passes the EP toxicity test.
    • 公开了从含有砷的含钨材料中回收钨的方法。 该方法包括用酸调节材料的水浆至小于约4的pH,以溶解钨的主要部分,向浆料中加入不溶性三价铁化合物以形成其中固相含有 砷的主要部分和可能存在的任何磷,以及含有主要部分钨的溶液相。 在从溶液中分离固体后,用酸将溶液调节至小于约2的pH,并向溶液中加入少量的六亚甲基四胺以沉淀出主要部分的钨,然后将沉淀物从 所得酒。 含有砷和磷的固相(如果有的话)可以与水和可溶性铁盐接触,以产生通过EP毒性试验的处理固体。
    • 6. 发明授权
    • Method for recovery of tungsten from spent catalysts
    • 从废催化剂中回收钨的方法
    • US5932184A
    • 1999-08-03
    • US271569
    • 1992-05-26
    • Michael J. MillerClarence D. Vanderpool
    • Michael J. MillerClarence D. Vanderpool
    • B01J38/00C01G41/00C22B7/00C22B34/36
    • C01G41/00C22B34/365C22B7/009Y02P10/214Y02P10/23Y02P10/234
    • A method for recovering tungsten from a tungsten containing spent catalyst comprises digesting the catalyst in aqueous sodium hydroxide solution wherein the mole ratio of the sodium hydroxide to the tungsten contained in the spent catalyst is from about 2.6 to about 4.2 and wherein the amount of water is sufficient to dissolve the subsequently produced sodium tungstate, at a temperature of at least about 90.degree. C. for a length of time of at least about 1 hour to convert greater than about 77% by weight of the tungsten contained in the spent catalyst to sodium tungstate and form a sodium tungstate solution thereof and a residue containing the balance of the starting tungsten, and separating the sodium tungstate solution from the residue. Essentially all of the tungsten is recovered as sodium tungstate by first grinding the catalyst prior to the digestion and by using a mole ratio of sodium hydroxide to tungsten of about 3.8 to 4.2.
    • 从含钨废催化剂中回收钨的方法包括在氢氧化钠水溶液中消化催化剂,其中氢氧化钠与废催化剂中所含的钨的摩尔比为约2.6至约4.2,其中水的量为 足以在随后产生的钨酸钠溶解在至少约90℃的温度下至少约1小时的时间,以将废催化剂中所含的钨的大于约77重量%转化为钠 形成钨酸钠溶液和含余量起始钨的残余物,并从残余物中分离出钨酸钠溶液。 通过在消化之前首先研磨催化剂和通过使用约3.8至4.2的氢氧化钠与钨的摩尔比,基本上所有的钨作为钨酸钠回收。
    • 7. 发明授权
    • Recovery of tungsten, scandium, iron, and manganese from tungsten
bearing material
    • 从钨轴承材料回收钨,钪,铁和锰
    • US4808384A
    • 1989-02-28
    • US145634
    • 1987-12-21
    • Clarence D. VanderpoolJudith A. LaddMartin B. MacInnisMary A. Fedorchak
    • Clarence D. VanderpoolJudith A. LaddMartin B. MacInnisMary A. Fedorchak
    • C01F17/00C22B3/08C22B3/28C22B3/38C22B34/36C22B47/00C22B59/00C01G41/00
    • C22B34/36C01F17/0006C22B3/0012C22B3/0068C22B3/08C22B47/00C22B59/00Y02P10/234
    • A process is disclosed for recovering tungsten, iron, and manganese from tungsten bearing material. The process involves digesting the material in a sufficient amount of sulfuric acid at a temperature of at least about 80.degree. C. for a sufficient time in the presence of coal as a reducing agent to form a digestion solution containing the major portion of the scandium, iron, and manganese and a digestion residue containing the major portion of the tungsten, followed by separating the solution from the residue. The major portion of the scandium can be extracted from the digestion solution with an organic solution consisting essentially of a mixture of tertiary alkyl primary amines which are present in an amount sufficient to extract the major portion of the scandium, and the balance an essentially aromatic solvent. The scandium is stripped from the organic with hydrochloric acid which is then separated from the stripped organic. The extraction can be accomplished by an organic solution consisting essentially of an extracting agent which is a dialkyl phosphoric acid and an essentially aromatic solvent. In this latter case, the stripping agent for the scandium is an aqueous solution of ammonium carbonate.
    • 公开了从含钨材料中回收钨,铁和锰的方法。 该方法包括在煤作为还原剂存在下,在至少约80℃的温度下将足量硫酸材料消化足够的时间以形成含有主要部分钪的消解溶液, 铁和锰以及含有主要部分钨的消化残渣,然后从残余物中分离溶液。 钪的主要部分可以从消解溶液中提取,其中有机溶液基本上由叔烷基伯胺的混合物组成,叔烷基伯胺以足以提取主要部分钪的量存在,余量为基本上为芳族溶剂 。 用盐酸从有机物中除去钪,然后与汽提的有机物分离。 提取可以通过主要由作为二烷基磷酸和基本上芳香族溶剂的萃取剂组成的有机溶液来完成。 在后一种情况下,用于钪的汽提剂是碳酸铵的水溶液。
    • 10. 发明授权
    • Production of pure molybdenum
    • 生产纯钼
    • US4605538A
    • 1986-08-12
    • US768387
    • 1985-08-22
    • Clarence D. Vanderpool
    • Clarence D. Vanderpool
    • C01G39/00C07F11/00
    • C07F11/005C01G39/00
    • A process is disclosed for producing pure molybdenum which involves contacting a molybdate solution with a true liquid alkaloid in an amount sufficient to form an alkaloid-molybdenum compound with essentially all of the molybdenum. The resulting alkaloid-treated solution is adjusted to a pH of from about 2 to 4 to form a precipitate consisting essentially of the compound and a mother liquor. The precipitate is then separated from the mother liquor and dissolved in ammonium hydroxide to form a two phase system consisting essentially of an alkaloid phase and a molybdenum phase followed by separation of the two phases. A pure ammonium molybdate compound is then crystallized from the molybdenum phase.
    • 公开了一种用于生产纯钼的方法,其涉及将钼酸盐溶液与足以形成基本上所有钼的生物碱 - 钼化合物的量的真实液体生物碱接触。 将所得生物碱处理的溶液调节至约2至4的pH,以形成基本上由化合物和母液组成的沉淀物。 然后将沉淀物与母液分离并溶解在氢氧化铵中以形成基本上由生物碱相和钼相组成的两相体系,随后分离两相。 然后将钼酸铵化合物从钼相中结晶出来。