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
    • 5. 发明授权
    • Recovery of cobalt and chromium
    • 回收钴和铬
    • US4608084A
    • 1986-08-26
    • US718257
    • 1985-04-01
    • Richard A. ScheithauerMichael J. MillerClarence D. VanderpoolMartin B. MacInnis
    • Richard A. ScheithauerMichael J. MillerClarence D. VanderpoolMartin B. MacInnis
    • C22B23/00C22B3/32C22B7/00C22B34/32C22B23/04
    • C22B23/0484C22B23/0423C22B3/0025C22B34/32C22B7/007Y02P10/234
    • A process is disclosed for recovering cobalt and chromium from a cobalt and chromium containing alloy. The process involves first digesting the alloy in concentrated hydrochloric acid at a sufficient temperature for a sufficient time to form a first solution containing the major portion of the cobalt, chromium, and any iron and nickel present in the alloy and a first solid and separating the first solution from the first solid. Oxalic acid is then added to the first solution in an amount sufficient to subsequently precipitate the major portion of the cobalt and any iron and nickel contained in the first solution followed by adjustment of the ph to from about 1 to about 2 with a base and maintaining the temperature below about 20.degree. for a sufficient time to form a second solid containing the major portion of the cobalt and the major portion of any iron and nickel which is present in the first solution and a second solution containing the major portion of the chromium which is present in the first solution and separation of the second solid from the second solution. The second solid is then washed with sufficient water to remove any water soluble impurities and separated from the resulting wash water. The resulting washed second solid is then contacted with a calcium chloride solution of sufficient calcium chloride concentration, at a sufficient temperature, for a sufficient time to form a third solution containing the major portion of the cobalt which was present in the second solid, and a third solid. The third solution is then separated from the third solid.
    • 公开了从含钴和铬的合金中回收钴和铬的方法。 该方法包括首先在足够的温度下将浓缩的合金中的合金消化足够的时间以形成含有合金中存在的钴,铬和任何铁和镍的主要部分的第一溶液和第一固体, 从第一个固体的第一个解决方案。 然后将草酸以足以随后沉淀出主要部分的钴和第一溶液中所含的任何铁和镍的量,然后用碱将ph调节至约1至约2,并保持 温度低于约20°足够的时间以形成第二固体,其含有钴的主要部分和存在于第一溶液中的任何铁和镍的主要部分和含有主要部分铬的第二溶液, 存在于第一溶液中并且将第二固体与第二溶液分离。 然后用足够的水洗涤第二固体以除去任何水溶性杂质并从得到的洗涤水中分离。 然后将所得洗涤后的第二固体在足够的温度下与足够氯化钙浓度的氯化钙溶液接触足够的时间以形成含有存在于第二固体中的钴的主要部分的第三溶液, 第三个固体。 然后将第三溶液与第三固体分离。
    • 6. 发明授权
    • Process for recovering tungsten as an ammoniacal tungstate compound in
which ammoniacal tungstate liquors are reclaimed
    • 用于回收钨作为氨基钨酸盐化合物的方法,其中回收了氨基钨酸盐液体
    • US5417945A
    • 1995-05-23
    • US795310
    • 1991-11-14
    • Richard G. W. GingerichJames N. ChristiniMartin C. VogtClarence D. VanderpoolMichael J. Miller
    • Richard G. W. GingerichJames N. ChristiniMartin C. VogtClarence D. VanderpoolMichael J. Miller
    • C01G41/00
    • C01G41/003C01G41/00
    • A process for recovering tungsten as an ammoniacal tungstate which comprises reacting a tungsten containing material with sodium hydroxide to produce sodium tungstate and forming a first aqueous sodium tungstate solution therefrom, crystallizing sodium tungstate from the first aqueous sodium tungstate solution, dissolving the resulting sodium tungstate crystals in an aqueous medium to form a second aqueous sodium tungstate solution, extracting tungsten from the second aqueous sodium tungstate solution with an organic extracting agent wherein the extracting agent containing tungsten is capable of being stripped of the extracted tungsten by ammonia, and thereafter stripping the extracted tungsten from the organic extracting agent with ammonia to form an ammoniacal tungstate solution, crystallizing a portion of the tungsten contained in the ammoniacal tungstate solution to form a two phase system wherein an ammoniacal tungstate compound comprises the first phase and wherein the resulting mother liquor containing the balance of the contained tungsten comprises the second phase, and repeating the process using the mother liquor as at least a portion of the aqueous medium to dissolve the sodium tungstate crystals.
    • 一种用于回收钨作为钨酸钨的方法,其包括使含钨材料与氢氧化钠反应以产生钨酸钠并从其中形成第一含水钨酸钠溶液,从第一钨酸钠水溶液中使钨酸钠结晶,将所得的钨酸钠晶体 在水性介质中形成第二钨酸钠水溶液,用有机萃取剂从第二钨酸钠水溶液中提取钨,其中含有钨的萃取剂能够用氨除去提取的钨,然后将提取的 钨从有机萃取剂中与氨反应形成一种氨基钨酸盐溶液,使一部分钨酸铵溶液中所含的钨结晶形成两相体系,其中氨基钨酸盐化合物包含第一相,其中所得的 含有所含钨的余量的母液包括第二相,并且重复使用母液作为至少一部分水性介质以溶解钨酸钠晶体的方法。
    • 9. 发明授权
    • Process for producing KS molybdenum
    • 生产KS钼的工艺
    • US5734960A
    • 1998-03-31
    • US297476
    • 1994-08-29
    • Thomas J. PatricianMichael J. MillerJames N. ChristiniMichael J. CheresnowskyVernon L. Carr, Jr.
    • Thomas J. PatricianMichael J. MillerJames N. ChristiniMichael J. CheresnowskyVernon L. Carr, Jr.
    • C22C1/04B22F1/00B22F3/12B22F9/22
    • C22C1/045
    • A process for producing potassium and silicon doped molybdenum (KS molybdenum). The process involves mixing an aqueous ammonium molybdate solution and a dilute aqueous potassium silicate solution. The molybdate solution has a pH and a specific gravity sufficient to promote formation of diammonium molybdate crystals in the mixture. Preferably, the pH is about 8.8-11.0 and the specific gravity is about 1.20-1.32. The amount of potassium silicate and the amount of potassium silicate solution are selected to provide predetermined amounts of potassium and silicon in the mixture, preferably about 800-1300 ppm potassium and about 500-1100 ppm silicon, both amounts based on the amount of molybdenum. The mixture is heated to aid dissolution of the potassium silicate and ammonium molybdate in said mixture and to produce a homogeneous solution of ammonium molybdate, potassium, and silicon. The ammonium dimolybdate doped with potassium and silicon is then crystallized out of solution and calcined, for example in an atmosphere of dissociated ammonia, to produce molybdenum dioxide doped with potassium and silicon. The doped molybdenum dioxide is reduced, for example in a flowing hydrogen atmosphere, to produce a doped molybdenum powder, which then may be pressed and sintered to full density.
    • 一种生产钾和硅掺杂钼(KS钼)的方法。 该方法包括混合钼酸铵水溶液和稀的硅酸钾水溶液。 钼酸盐溶液具有足以促进混合物中钼酸铵晶体形成的pH和比重。 优选地,pH为约8.8-11.0,比重为约1.20-1.32。 选择硅酸钾的量和硅酸钾溶液的量以在混合物中提供预定量的钾和硅,优选约800-1300ppm钾和约500-1100ppm硅,两者都基于钼的量。 将混合物加热以帮助硅酸钾和钼酸铵在所述混合物中的溶解,并产生钼酸铵,钾和硅的均匀溶液。 然后将掺杂有钾和硅的二钼酸铵从溶液中结晶出来并煅烧,例如在解离的氨气氛中,生成掺有钾和硅的二氧化钼。 掺杂的二氧化钼例如在流动的氢气氛中被还原,以产生掺杂的钼粉末,然后可将其压制并烧结至全密度。