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    • 14. 发明授权
    • Electrochemical leaching of soil
    • 电化学浸出土壤
    • US5876590A
    • 1999-03-02
    • US772475
    • 1996-12-23
    • Thomas S. SnyderDale L. Keairns
    • Thomas S. SnyderDale L. Keairns
    • B01D61/44B09C1/02B09C1/08C02F1/467C02F1/469
    • B09C1/085B01D61/44B09C1/02C02F1/4678C02F1/469C02F2201/46115C02F2201/46185
    • An electrochemical leaching system for cleaning contaminated fines. The system has a waste vessel for receiving and holding a contaminated fines and lixiviant mixture. On a side of the waste vessel is an anolyte vessel holding an anolyte fluid. An anolyte barrier separates the waste and anolyte vessels. On an opposite side of the waste vessel is a catholyte vessel holding a catholyte fluid. A catholyte barrier separates the waste and catholyte vessels. A potential between an anode in the anolyte vessel and a cathode in the catholyte vessel ionizes the fines contaminants into anionic and cationic contaminants in the lixiviant. The anolyte and catholyte barriers allow the anionic and cationic contaminants, respectively, to flow from the lixiviant and into the anolyte and catholyte fluids in their respective vessels without allowing bulk transfer therebetween. The anionic and cationic contaminants are then removed from the anolyte and catholyte fluids. A cleaner lixiviant and fines exits the system.
    • 用于清洁污染细粉的电化学浸出系统。 该系统具有用于接收和保持受污染的细粒和浸渍混合物的废物容器。 在废物容器的一侧是保持阳极电解液的阳极电解液容器。 阳极电解屏障将废物和阳极液容器分开。 废物容器的另一侧是容纳阴极液的阴极电解液容器。 阴极电解屏障将废物和阴极电解液分离。 阳极电解液容器中的阳极与阴极电解液容器中的阴极之间的电位将细粉污染物离子化为浸出液中的阴离子和阳离子污染物。 阳极电解液和阴极电解液屏障允许阴离子和阳离子污染物分别从其浸泡液流入其各自容器中的阳极电解液和阴极液,而不允许其间的块体转移。 然后从阳极电解液和阴极液中除去阴离子和阳离子污染物。 更清洁的洗涤剂和罚款退出系统。
    • 16. 发明授权
    • Decontamination of radioactive metals
    • 放射性金属的去污
    • US5262019A
    • 1993-11-16
    • US991807
    • 1992-12-16
    • Thomas S. SnyderLaura J. AyersChuck A. CooneyGregory F. BorisDwight F. GoadKevin D. RobbinsDarrell B. Watkins
    • Thomas S. SnyderLaura J. AyersChuck A. CooneyGregory F. BorisDwight F. GoadKevin D. RobbinsDarrell B. Watkins
    • G21F9/06G21F9/30C25C1/06
    • G21F9/30G21F9/06
    • Technetium-contaminated nickel is decontaminated by electrolytically dissolving nickel having a gross beta activity of at least about 74 Bq in a sulfuric acid solution having a pH between about 0.5 and 2.0. The applied voltage is from 2.0 v/cell to 5.0 v/cell for dissolving the nickel and contaminants while cathodically producing hydrogen gas. Technetium (+4) species in the acid solution is oxidized to the technetium (+7) species. The pH of the technetium-containing acid solution is adjusted to between 2.5 to 4.5. Particulates in the acid solution are filtered from the solution for reducing the gross beta activity of the acid solution to less than about 50 Bq/gm. Radioactive ions (including technetium complexes) are sorbed in an anionic exchanger and a cationic exchanger for reducing the gross beta activity of the acid solution to less than about 20 Bq/gm. After verifying the gross beta activity of the acid solution, the acid solution is either recycled or charged to a electrowinning step. Acid solution having an activity of more than about 20 Bq/gm is recycled to upstream of the anion exchanger and the cationic exchanger. Acid solution having a gross beta activity of less than about 20 Bq/gm is charged to the electrowinning step. Nickel is plated at a voltage of about 2 v/cell to about 6 v/cell while oxygen gas is anodically generated. The pH of barren metal acid solution from the electrowinning step is reduced to less than about 2 and the barren metal acid solution is recycled for dissolving additional contaminated nickel.
    • 锝污染的镍通过在具有约0.5至2.0的pH的硫酸溶液中电解溶解至少约74Bq的总β活性的镍来净化。 施加的电压为2.0v / cell至5.0v / cell,用于溶解镍和污染物,同时阴极生产氢气。 酸溶液中的锝(+4)物质被氧化成锝(+7)种。 将含锝酸溶液的pH调节至2.5至4.5。 从溶液中过滤酸溶液中的颗粒,以将酸溶液的总β活性降低至小于约50Bq / gm。 放射性离子(包括锝络合物)在阴离子交换剂和阳离子交换剂中吸附,用于将酸溶液的总β活性降低至小于约20Bq / gm。 在验证酸溶液的总β活性后,将酸溶液回收或加入电解提取步骤。 具有大于约20Bq / gm活性的酸溶液被再循环到阴离子交换剂和阳离子交换剂的上游。 将具有小于约20Bq / gm的总β活性的酸溶液加入到电解提取步骤中。 镍以约2V /电池至约6V /电池的电压进行电镀,同时阳极生成氧气。 来自电解沉积步骤的贫金属酸溶液的pH降低到小于约2,并且再循环贫金属酸溶液以溶解额外的污染的镍。
    • 17. 发明授权
    • Method for chromatographically recovering scandium and yttrium
    • 色谱回收钪和钇的方法
    • US5045209A
    • 1991-09-03
    • US587191
    • 1990-09-24
    • Thomas S. SnyderRichard A. Stoltz
    • Thomas S. SnyderRichard A. Stoltz
    • B01D15/08C22B59/00G01N30/58
    • B01D15/1892C22B59/00B01D15/362B01D15/426G01N30/58Y02P10/212
    • Scandium and yttrium present in sand is recovered from the residue pulled from sand chlorinators. The residue is digested with an acid to produce a liquid containing scandium, yttrium, sodium, calcium and at least one radioactive metal of the group consisting of radium, thorium and uranium. The metal-containing liquid is then fed through a cation exchanger. The cation exchanger is eluted with an acid to produce eluate functions containing at least partially separated metals. A first eluate fraction contains at least half of the calcium and the sodium, a second eluate fraction contains at least half of the radioactive metals, a third eluate fraction contains at least half of the scandium and a fourth eluate fraction contains at least half of the yttrium which were contained in the metal-containing feed.
    • 沙子中存在的钪和钇从从氯化钠洗涤剂中抽出的残余物中回收。 残余物用酸消化以产生含有钪,钇,钠,钙和至少一种由镭,钍和铀组成的组的放射性金属的液体。 然后将含金属液体通过阳离子交换器进料。 阳离子交换剂用酸洗脱以产生含有至少部分分离的金属的洗脱液功能。 第一洗脱液组分含有至少一半的钙和钠,第二洗脱液组分含有至少一半的放射性金属,第三洗脱液组分含有至少一半的钪,第四洗脱液组分含有至少一半的 包含在含金属的进料中的钇。