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    • 1. 发明授权
    • Europium-doped yttrium oxide phosphor
    • 铕掺杂氧化钇荧光体
    • US5525259A
    • 1996-06-11
    • US866880
    • 1992-04-02
    • Robin W. MunnRichard G. W. GingerichJames Morse
    • Robin W. MunnRichard G. W. GingerichJames Morse
    • C09K11/02C09K11/77C09K11/78H01J61/44
    • H01J61/44C09K11/025C09K11/7787
    • Disclosed is a large size Y.sub.2 O.sub.3 :Eu lamp phosphor as a red component for a water degradation resistant blend of fluorescent phosphors having large sized green phosphor particles and the method for making by blending yttrium oxide and europium oxide with fluxing agents, firing, milling the fired phosphor; sieving the milled phosphor to obtain a phosphor with an average particle size greater than about 5 by Coulter Counter to produce a sieved phosphor, and encapsulated a conformal coating of gamma alumina on said sieved phosphor by vapor chemical vapor deposition to form a resulting coated Y.sub.2 O.sub.3 :Eu phosphor with additional phosphor components including a green phosphor to form a lamp phosphor blend, and applying the blend to a lamp as a water based suspension.
    • 公开了一种大尺寸的Y 2 O 3:Eu灯荧光体,作为具有大尺寸绿色荧光体颗粒的荧光荧光体的耐水分降解混合物的红色成分,以及通过将氧化钇和氧化铕与助熔剂混合来制造的方法, 磷; 筛分研磨的磷光体,通过库尔特计数器获得平均粒径大于约5的磷光体,以产生筛分的荧光体,并通过蒸气化学气相沉积在所述筛分的磷光体上包封γ氧化铝的保形涂层,以形成所得的涂覆的Y 2 O 3: Eu荧光粉,其具有包括绿色磷光体的另外的荧光体组分以形成灯荧光体共混物,并将该混合物作为水基悬浮液施加到灯上。
    • 3. 发明授权
    • Purification of molybdenum trioxide
    • 三氧化钼的纯化
    • US4643884A
    • 1987-02-17
    • US846170
    • 1986-03-31
    • Michael J. CheresnowskyTimothy A. BrunelliRobin W. Munn
    • Michael J. CheresnowskyTimothy A. BrunelliRobin W. Munn
    • C01G39/02
    • C01G39/02C01P2006/80
    • A process is disclosed for removing potassium from relatively impure molybdenum trioxide. The process involves contacting the impure molybdenum trioxide containing greater than about 600 weight parts potassium per million with a first acid leach which consists essentially of nitric acid and ammonium nitrate at a temperature of at least about 50.degree. C. for a sufficient time and at above a 2 molar concentration of said nitric acid and an ammonium nitrate concentration of from about 1.5 to about 2 molar in said first acid leach to solubilize the major portion of the potassium and form a once leached molybdenum trioxide containing the remaining portion of the potassium which is separated from the resulting potassium containing acid leach and contacted with a second leach solution substantially similar to the first acid leach followed by separating the resulting twice leached molybdenum trioxide from the resulting potassium containing second leach. The twice leached molybdenum trioxide is contacted with sufficient water to remove any residual impurities followed by removal of the resulting wash water.
    • 公开了从相对不纯的三氧化钼中除去钾的方法。 该方法包括使含有大于约600重量份百万分之比的钾的不纯三氧化钼与至少约50℃的温度下基本上由硝酸和硝酸铵组成的第一酸浸液接触足够的时间和在上述 在所述第一酸浸液中,所述硝酸浓度为2摩尔浓度,硝酸铵浓度为约1.5至约2摩尔,以溶解钾的主要部分,并形成含有剩余部分钾的一次浸出的三氧化钼 与所得的含钾酸浸出物分离,并与基本上类似于第一酸浸提液的第二浸出溶液接触,随后从得到的含钾第二浸出物中分离得到的两次浸提的三氧化钼。 将两次浸提的三氧化钼与足够的水接触以除去任何残余杂质,然后除去所得洗涤水。
    • 4. 发明授权
    • Production of ammonium tetrathiomolybdate
    • 四硫代钼酸铵的生产
    • US4604278A
    • 1986-08-05
    • US734985
    • 1985-05-17
    • Kenneth T. ReillyRobin W. MunnHenry E. HoffmanAlan D. Douglas
    • Kenneth T. ReillyRobin W. MunnHenry E. HoffmanAlan D. Douglas
    • C01G39/00C01G39/06
    • C01G39/006C01G39/06
    • A process is disclosed for producing ammonium tetrathiomolybdate. The process involves reacting an ammoniacal molybdate solution with hydrogen sulfide gas, the solution and the gas being in a closed system and the flow of the gas being regulated at an elevated pressure to form a slurry consisting essentially of a solid essentially all of which is ammonium tetrathiomolybdate containing a portion of the starting molybdenum and a mother liquor containing the balance of the molybdenum. The slurry is then cooled to ambient temperature and the solid is removed from the major portion of the mother liquor. The solid is then washed with water and with alcohol followed by removal of the resulting respective water and alcohol washes to remove the remaining portion of the mother liquor and soluble impurities from the solid. The resulting washed solid is then dried at ambient temperature to form the final ammonium tetrathiomolybdate.
    • 公开了用于生产四硫代钼酸铵的方法。 该方法包括使氨基钼酸盐溶液与硫化氢气体反应,溶液和气体处于封闭系统中,并且气体的流动在升高的压力下调节以形成基本上由固体组成的浆料,其基本上全部为铵 含有起始钼的一部分的四硫钼酸盐和含有余量的钼的母液。 然后将浆液冷却至环境温度,并将固体从母液的主要部分除去。 然后将固体用水和醇洗涤,然后除去所得的各自的水和醇洗涤剂以从固体中除去母液的剩余部分和可溶性杂质。 然后将所得洗涤的固体在环境温度下干燥以形成最终的四硫代钼酸铵。
    • 6. 发明授权
    • Procedure for controlling powder fluidity
    • 控制粉末流动性的程序
    • US4915976A
    • 1990-04-10
    • US279611
    • 1988-12-05
    • Doris L. BrownCharles F. ChenotDeborah V. LutzRobin W. Munn
    • Doris L. BrownCharles F. ChenotDeborah V. LutzRobin W. Munn
    • B01J8/00B01J8/24
    • B01J8/1809B01J8/008B01J2208/0061
    • A process is disclosed for applying a lubricant to a powdered material to control the fluidity of the powdered material. In the process one first obtains at least x number of samples of the powdered material without lubricant. Thereafter, increasing amounts of lubricant are applied to x-1 number of the samples. The bulk and tap densities of the samples are then measured and the Hausner ratio from the densities is calculated. The Hausner ratio versus the concentration of the lubricant in the powder samples is plotted and the concentrations of the minima lubricant in the powder samples at the point of the plot obtained in step e are determined. The concentration of lubricant determined in step f is applied to the remainder of the powdered material whereby an operational level of fluidity of the powder is achieved.
    • 公开了一种将润滑剂施加到粉末材料以控制粉末材料的流动性的方法。 在该过程中,首先获得至少x个样品的粉末材料,而不需要润滑剂。 此后,将增加量的润滑剂施加到x-1个样品。 然后测量样品的体积和抽头密度,并计算来自密度的Hausner比。 绘制Hausner比与粉末样品中润滑剂浓度的关系,并确定在步骤e中获得的图中点处的粉末样品中最小润滑剂的浓度。 在步骤f中确定的润滑剂的浓度被施加到粉末材料的其余部分,由此实现粉末的流动性的操作水平。