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    • 3. 发明授权
    • Method of improving the criticality safety in a liquid-liquid extraction
process for spent nuclear fuel or breeder reactor materials
    • 提高废核燃料或增殖反应堆材料液液萃取过程中临界安全性的方法
    • US4871478A
    • 1989-10-03
    • US117848
    • 1987-11-09
    • Georg PetrichHelmut Schmieder
    • Georg PetrichHelmut Schmieder
    • G21C19/42G21C19/46G21F9/12
    • G21F9/125G21C19/46Y02W30/883
    • A process for the extraction of uranium and plutonium from spent nuclear fuels or breeder reactor materials. The spent nuclear fuels or breeder reactor materials are dissolved in nitric acid to provide an aqueous acid solution containing uranium, plutonium, neptunium, other transuranium elements, fission products, corrosion products, activation products and other contamination products. This aqueous acid solution is fed, as an aqueous phase, at a controllable flow rate into a liquid-liquid extraction apparatus also having an organic solvant phase flowing at a controllable rate. The organic phase contains an extraction agent. The temperature of solutions in the extraction apparatus and/or the concentration of the aqueous acid solution before the said aqueous acid solution is fed into the extraction apparatus, is adjusted to satisfy the following inequality: ##EQU1## where T.sub.E =the temperature of the solutions in the extractor (.degree.C.);U.sub.f =the uranium concentration of the feed solution (g/l);Pu.sub.f =the plutonium concentration of the feed solution (g/l);H.sub.f =nitric acid concentration of the feed solution (M/l); ande=base of the natural logarithm system.
    • 从废核燃料或增殖反应堆材料中提取铀和钚的过程。 将废核燃料或增殖反应堆材料溶解在硝酸中以提供含有铀,钚,ium,其他铀元素,裂变产物,腐蚀产物,活化产物和其他污染产物的酸性水溶液。 该酸性水溶液作为水相以可控的流速进料到液体 - 液体萃取装置中,该装置也具有以可控速率流动的有机溶剂相。 有机相含有提取剂。 将提取装置中的溶液的温度和/或酸性水溶液的浓度进料到萃取装置中,以满足以下不等式:TE> 401 +(0.06676 Uf-0.3367 Puf- 327.4 Hf)x ex0.00008179(Uf + Puf)HfxHf-0.9593其中TE =萃取器中溶液的温度(℃); Uf =进料溶液的铀浓度(g / l); Puf =进料溶液的钚浓度(g / l); Hf =进料溶液的硝酸浓度(M / l); e =自然对数系统的基数。
    • 6. 发明授权
    • Countercurrent extraction column for liquid-liquid extraction
    • 液 - 液萃取逆流萃取柱
    • US4101408A
    • 1978-07-18
    • US757062
    • 1976-12-30
    • Helmut SchmiederHubert GoldackerWerner Roos
    • Helmut SchmiederHubert GoldackerWerner Roos
    • B01D11/04B01D59/24C01G99/00C22B3/02C22B60/02C25B1/00C25C7/00
    • C01G99/006B01D11/0419C22B3/02C22B60/026C25B1/00Y02P10/234
    • A countercurrent extraction column for a liquid-liquid extraction of two phases which are insoluble in each other with simultaneous electrolysis. The column comprises an outer tube, an inner tube within the outer tube, with the inner tube dividing the column into an inner anode chamber and an outer cathode chamber which encloses the anode chamber without the use of a diaphragm. A plurality of bores establish communication between the anode chamber and the cathode chamber. An anode is provided in the anode chamber and a cathode is provided in the cathode chamber. A hollow sheet metal cylinder is disposed around the inner tube in the area of the bores between the cathode chamber and the anode chamber. The cylinder acts as a cathode cylinder member and is chargeable in its interior by one of the phases through bores located at the top of the cathode cylinder. Sheet metal strips are attached in a radially inwardly extending manner to the interior surface of the cathode cylinder.
    • 一种用于液相萃取的逆流提取塔,两相不溶于同时电解。 该柱包括外管,外管内管,内管将柱分成内阳极室和外阳极室,其不使用隔膜而封闭阳极室。 多个孔在阳极室和阴极室之间建立连通。 阳极设置在阳极室中,阴极设置在阴极室中。 在阴极室和阳极室之间的孔的区域内围绕内管设置中空的金属板。 气缸用作阴极筒构件,并且可通过位于阴极筒顶部的孔之一通过其中一个相位将其内部充电。 钣金条以径向向内延伸的方式附接到阴极筒的内表面。
    • 10. 发明授权
    • Method for purifying actinides which are in low oxidation states
    • 纯化处于低氧化态的锕系元素的方法
    • US4021313A
    • 1977-05-03
    • US624106
    • 1975-10-20
    • Helmut HausbergerHubert GoldackerHelmut Schmieder
    • Helmut HausbergerHubert GoldackerHelmut Schmieder
    • C01G43/00C01G56/00C01G99/00C22B3/00C22B3/26C22B60/02C22B61/00C25B1/00G21C19/46G21F9/00G21F9/06C25C3/34
    • C25B1/00C01G43/00C01G56/004C01G56/008C01G99/006C22B60/026
    • A method is provided for purifying actinides which are present in a low oxidation state in aqueous solution. The actinides are purified of fission products by extracting the actinides from aqueous solution while confining the fission products to the aqueous solution. The actinides that are purified are selected from the group of uranium (IV), neptunium (IV) and plutonium (III). An aqueous nitric acid solution containing the actinides, hydrazine nitrate or hydroxyl ammonium nitrate, as well as fission products is initially subjected to an electrolysis voltage. If Pu (III) is involved, the electrolysis voltage is below the voltage at which oxygen develops at the anode and anodically oxidizes the Pu (III) to Pu (IV). The Pu (IV) which is formed is transferred by means of an organic extraction agent from the aqueous solution to an organic phase. The organic phase is then separated and used for the plutonium recovery process. If U (IV) and/or Np (IV) are involved, the aqueous nitric acid solution is initially subjected to an electrolysis voltage in the vicinity of the voltage at which oxygen develops at the anode or higher to anodically oxidize the U (IV) to U (VI) and the Np (IV) to Np (VI). The U (VI) and/or Np (VI) which is formed is transferred by means of an organic extraction agent from the aqueous phase to the organic phase. The organic phase is then separated and used for the uranium or neptunium recovery process.
    • 提供了一种用于纯化在水溶液中以低氧化态存在的锕系元素的方法。 锕系元素通过从水溶液中提取锕系元素而将裂变产物限制在水溶液中来纯化裂变产物。 纯化的锕系选自铀(IV),ium(IV)和钚(III)。 含有锕系元素,硝酸肼或硝酸铵的硝酸水溶液以及裂变产物最初经受电解电压。 如果涉及Pu(III),则电解电压低于在阳极处产生氧气的电压,并将Pu(III)阳极氧化为Pu(IV)。 形成的Pu(IV)通过有机萃取剂从水溶液中转移到有机相中。 然后将有机相分离并用于钚回收过程。 如果涉及U(IV)和/或Np(IV),则硝酸水溶液最初经受在阳极或更高氧发生的电压附近的电解电压,以阳极氧化U(IV) 到U(VI)和Np(IV)到Np(VI)。 形成的U(VI)和/或Np(VI)通过有机萃取剂从水相转移到有机相中。 然后将有机相分离并用于铀或铀回收过程。