Multicomponent fluid feed apparatus with preheater and mixer for a high
temperature chemical reactor
    1.
    发明授权
    Multicomponent fluid feed apparatus with preheater and mixer for a high temperature chemical reactor 失效
    具有高温化学反应器预热器和混合器的多组分流体输送装置

    公开(公告)号:US5935528A

    公开(公告)日:1999-08-10

    申请号:US783512

    申请日:1997-01-14

    摘要: A multicomponent fluid feed apparatus is disclosed that independently preheats and then mixes two or more fluid streams being introduced into a high temperature chemical reactor to promote more rigorous and complete reactions using assemblies of inert tubular elements and an integral mixing orifice plate. The design allows use of ceramic and speciality alloy materials for high temperature service with particularly corrosive halide feeds such as UF.sub.6 and HF. Radiant heat transfer to the tubular elements from external means gives the necessary system high temperatures without excessive temperatures to cause material failure. Preheating of the gaseous reactants in a separate step prior to mixing and injecting the gaseous reactants into a high temperature chemical reactor was found to provide an improved thermal conversion of UF.sub.6 to uranium oxides.

    摘要翻译: 公开了一种多组分流体输送装置,其独立地预热然后将引入到高温化学反应器中的两种或更多种流体流混合,以使用惰性管状元件和整体混合孔板的组件来促进更严格和完整的反应。 该设计允许使用陶瓷和特种合金材料进行高温维护,特别是腐蚀性卤化物进料如UF6和HF。 从外部装置向管状元件的辐射热传递给出必要的系统高温,而没有过多的温度导致材料失效。 发现在气态反应物混合并将气态反应物注入高温化学反应器之前,在单独的步骤中预热气态反应物以提供UF 6与氧化铀的改进的热转化。

    UF.sub.6 -Recovery process utilizing desublimation
    2.
    发明授权
    UF.sub.6 -Recovery process utilizing desublimation 失效
    UF6 - 利用desublimation的恢复过程

    公开(公告)号:US4546611A

    公开(公告)日:1985-10-15

    申请号:US564113

    申请日:1983-12-21

    IPC分类号: B01D7/02 F17C13/00

    CPC分类号: B01D7/02

    摘要: The invention is a UF.sub.6 -recovery process of the kind in which a stream of substantially pure gaseous UF.sub.6 is directed through an externally chilled desublimer to convert the UF.sub.6 directly to an annular solid ring adhering to the interior wall of the desublimer. After accumulation of a desired amount of solid UF.sub.6, the desublimer is heated to liquefy the solid. Subsequently, the liquid is recovered from the desublimer. It has been found that during the heating operation the desublimer is subjected to excessive mechanical stresses. In addition, it has been found that the incorporation of a very small percentage of relatively noncondensable, nonreactive gas (e.g., nitrogen) in the UF.sub.6 input to the desublimer effects significant decreases in the stresses generated during the subsequent melting operation. This modification to the process provides valuable advantages in terms of reduced hazard, lower operating costs for the desublimer, and increased service life for the desublimer and its auxiliaries. The new process is especially suitable for the recovery of enriched UF.sub.6 from high-speed UF.sub.6 gas-centrifuge cascades.

    摘要翻译: 本发明是一种UF6回收方法,其中基本上纯的气态UF6流被引导通过外部冷却的均质器,以将UF6直接转换成附着在均质器内壁的环形固体环。 在堆积所需量的固体UF6之后,将均质化合物加热以使固体液化。 随后,从均质器中回收液体。 已经发现,在加热操作期间,均质器受到过大的机械应力。 此外,已经发现,将非常少百分比的相对不可缩短的非反应性气体(例如氮)引入到均质合子的UF6输入中,在随后的熔融操作期间产生的应力的作用显着降低。 对该方法的这种修改在减少危害,降低发行人的运营成本以及延长其分配器及其辅助设备的使用寿命方面提供了宝贵的优势。 新工艺特别适用于从高速UF6气体离心机级联回收富集的UF6。

    Method for improving dissolution efficiency in gas-absorption and liquid
extraction processes
    3.
    发明授权
    Method for improving dissolution efficiency in gas-absorption and liquid extraction processes 失效
    提高气体吸收和液体萃取过程溶解效率的方法

    公开(公告)号:US4305735A

    公开(公告)日:1981-12-15

    申请号:US111495

    申请日:1980-01-11

    摘要: This invention is a method for improving dissolution efficiency in processes in which a feed fluid is introduced to a zone where it is contacted with a liquid solvent for preferentially removing a component of the feed and where part of the solvent so contacted undergoes transfer into the feed fluid to saturate the same. It has been found that such transfer significantly impairs dissolution efficiency. In accordance with the invention, an amount of the above-mentioned solvent is added to the feed fluid being introduced to the contact zone, the solvent being added in an amount sufficient to effect reduction or elimination of the above-mentioned transfer. Preferably, the solvent is added to the feed fluid in an amount saturating or supersaturating the feed fluid under the conditions prevailing in the contact zone.

    摘要翻译: 本发明是一种提高溶解效率的方法,其中将进料流体引入到与液体溶剂接触的区域中以优先除去进料成分的区域中,并且其中一部分如此接触的溶剂转移到进料中 流体饱和一样。 已经发现这种转移显着地损害溶解效率。 根据本发明,将一定量的上述溶剂加入到引入到接触区的进料流体中,加入的溶剂的量足以减少或消除上述转移。 优选地,在进料流体中以在接触区域中主要的条件下使进料流体饱和或过饱和的量加入溶剂。

    Method for the control of the composition and physical properties of
solid uranium oxides
    4.
    发明授权
    Method for the control of the composition and physical properties of solid uranium oxides 失效
    控制固体氧化铀的组成和物理性质的方法

    公开(公告)号:US5875385A

    公开(公告)日:1999-02-23

    申请号:US783264

    申请日:1997-01-15

    IPC分类号: C01G43/01 C01G43/025

    摘要: The present invention provides a method for varying and controlling the chemical composition and physical properties of the uranium oxide solids produced by the thermal conversion of UF.sub.6. The method allows the production of predominantly UO.sub.2, U.sub.3 O.sub.8, or UO.sub.3 interchangeably from the same reactor simply by controlling the hydrogen and oxygen contents of the feed relative to uranium. The temperature profile of the thermal reactor is established by specifying the preheat of the feed prior to mixing, the feed composition, and the reactor wall temperature to thus vary and control the physical properties of the resulting solids according to the end use of the uranium product.

    摘要翻译: 本发明提供了一种用于改变和控制由UF6的热转化产生的氧化铀固体的化学组成和物理性质的方法。 该方法允许主要通过相对于铀控制进料的氢和氧含量从相同的反应器互换地生产UO2,U3O8或UO3。 热反应器的温度曲线是通过在混合之前指定进料的预热,进料组成和反应器壁温度来确定的,从而根据铀产物的最终用途改变和控制所得固体的物理性能 。

    Thermal process for the conversion of uranium hexafluoride
    5.
    发明授权
    Thermal process for the conversion of uranium hexafluoride 失效
    用于六氟化铀转化的热处理

    公开(公告)号:US5752158A

    公开(公告)日:1998-05-12

    申请号:US657937

    申请日:1996-05-30

    IPC分类号: C01B7/19 C01G43/025 C01G43/01

    摘要: A single-step process for producing solid uranium oxide and gaseous HF from UF.sub.6 which comprises bringing together two gaseous reactant streams, one of said streams comprising UF.sub.6 optionally admixed with oxygen as O.sub.2, and the second reactant stream comprising a mixture of hydrogen as H.sub.2 or as a hydrogen-containing compound and oxygen as an oxygen-containing compound, said gaseous reactant streams being brought together at a temperature and composition such that the UF.sub.6 is converted rapidly by flame reaction into readily separable solid uranium oxide and a gaseous HF product.

    摘要翻译: 用于从UF6生产固体氧化铀和气态HF的单步方法,其包括将两种气态反应物流,包含UF 6的所述物流之一任选与氧气作为O 2混合,以及包含氢气作为H 2的混合物的第二反应物流 作为含氢化合物和作为含氧化合物的氧气,所述气态反应物流在温度和组成使得UF 6通过火焰反应迅速转化成容易分离的固体氧化铀和气态HF产物的情况下聚在一起。

    Gas-absorption process
    6.
    发明授权
    Gas-absorption process 失效
    吸气过程

    公开(公告)号:US4129425A

    公开(公告)日:1978-12-12

    申请号:US816575

    申请日:1977-07-18

    IPC分类号: B01D3/32 B01D53/14 B01D53/16

    摘要: This invention is an improved gas-absorption process for the recovery of a desired component from a feed-gas mixture containing the same. In the preferred form of the invention, the process operations are conducted in a closed-loop system including a gas-liquid contacting column having upper, intermediate, and lower contacting zones. A liquid absorbent for the desired component is circulated through the loop, being passed downwardly through the column, regenerated, withdrawn from a reboiler, and then recycled to the column.A novel technique is employed to concentrate the desired component in a narrow section of the intermediate zone. This technique comprises maintaining the temperature of the liquid-phase input to the intermediate zone at a sufficiently lower value than that of the gas-phase input to the zone to effect condensation of a major part of the absorbent-vapor upflow to the section. This establishes a steep temperature gradient in the section. The stripping factors below this section are selected to ensure that virtually all of the gases in the downflowing absorbent from the section are desorbed. The stripping factors above the section are selected to ensure re-dissolution of the desired component but not the less-soluble diluent gases. As a result, a peak concentration of the desired component is established in the section, and gas rich in that component can be withdrawn therefrom.The new process provides important advantages. The chief advantage is that the process operations can be conducted in a single column in which the contacting zones operate at essentially the same pressure.

    摘要翻译: 本发明是一种改进的气体吸收方法,用于从含有该组分的原料 - 气体混合物回收所需组分。 在本发明的优选形式中,工艺操作在包括具有上,中,下接触区的气 - 液接触塔的闭环系统中进行。 用于所需组分的液体吸收剂循环通过循环,向下通过柱,再生,从再沸器中取出,然后再循环至塔中。