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    • 5. 发明申请
    • Method and apparatus for determining the progress of a chemical reaction in a furnace and for controlling the reaction
    • 用于确定炉中化学反应进程和控制反应的方法和装置
    • US20030064519A1
    • 2003-04-03
    • US10203445
    • 2002-08-08
    • Andre Fuegier
    • C01G043/01G01N033/00
    • G21C3/623C01G43/025C01P2006/80G01N33/0036Y02E30/38Y10T436/12Y10T436/153333Y10T436/16Y10T436/207497
    • A substance in a condensed state, for example a powdered solid, is in continuous movement in the longitudinal direction (6) of a furnace (4, 5). A reactive gas mixture is brought into contact with the substance in the condensed state. A plurality of samples of the gaseous mixture are removed at a plurality of reference points (14) spaced apart from one another along the longitudinal direction (6) of the furnace (4, 5); each of the gas samples is analyzed outside the furnace to determine the composition of the gas mixture and for each point (14), the extent of a chemical reaction between the condensed substance and the reactive gas mixture is deduced from the composition of the gas mixture at each of the reference points (14). In particular, the apparatus comprises a sampling and injection rod (10) introduced into the furnace (4, 5) and disposed in its longitudinal direction (6). The invention is of particular application to modeling a rotary furnace (4, 5) for converting uranium oxyfluoride into uranium oxides and for controlling the conversion reaction in the furnace (4, 5).
    • 处于冷凝状态的物质,例如粉末状固体,在炉(4,5)的纵向(6)上连续运动。 使反应性气体混合物与冷凝状态的物质接触。 多个样品的气体混合物在沿着炉子4,5的纵向方向(6)彼此间隔开的多个参考点(14)处被去除; 在炉外分析每个气体样品以确定气体混合物的组成,并且对于每个点(14),从气体混合物的组成推导出冷凝物质和反应性气体混合物之间的化学反应的程度 在每个参考点(14)处。 特别地,该装置包括被引入炉(4,5)中并沿其纵向方向(6)设置的取样和注入杆(10)。 本发明特别适用于将用于将铀氧氟化物转化为铀氧化物并用于控制炉子(4,5)中的转化反应的旋转炉(4,5)的建模。
    • 10. 发明授权
    • Uranium oxide production
    • 氧化铀生产
    • US5723100A
    • 1998-03-03
    • US592337
    • 1996-03-07
    • Robert CarterJohn Terry Semeraz
    • Robert CarterJohn Terry Semeraz
    • G21C3/62C01G43/01C01G43/025
    • C01G43/025C01P2006/12C01P2006/80
    • A process for the production of a uranium oxide in which UF.sub.6 is converted by reaction with steam into UO.sub.2 F.sub.2 in a first step and by further reaction of UO.sub.2 F.sub.2 with steam and/or hydrogen in a second step to produce an oxide of uranium, the process being carried out in an apparatus comprising a single kiln vessel having a first region, having UF.sub.6 and steam inlets, wherein the fast step may be carried out, and a second region wherein the said second step may be carried out, which process includes the further steps of analysing the oxide of uranium produced to determine the mount of fluoride present and the oxygen to uranium (O/U) ratio therein, and, where the level of fluoride present is unacceptably high, recycling the oxide of uranium to the said second region to produce an oxide of uranium having a lower fluoride content and oxygen to uranium ratio and wherein the said oxide of uranium having the unacceptably high fluoride content is fed into the first region of the vessel, in the absence of any feeding of UF.sub.6 or steam thereto, and conveyed by conveying means directly into the second region of the vessel.
    • PCT No.PCT / GB95 / 01281 Sec。 371日期:1995年3月7日 102(e)1995年3月7日PCT PCT。1995年6月2日PCT公布。 第WO95 / 33689号公报 日期1995年12月14日一种生产氧化铀的方法,其中UF6在第一步骤中通过与蒸汽反应转化成UO2F2而转化,并且在第二步中进一步与UO2F2与蒸汽和/或氢反应以产生氧化铀 铀,该方法在包括具有UF 6和蒸汽入口的第一区域的单个窑容器的装置中进行,其中可执行快速步骤,以及可执行所述第二步骤的第二区域, 方法包括进一步分析生产的铀氧化物以确定氟化物存在量和其中氧铀(O / U)比率的氧化物,并且当存在的氟化物水平不可接受地高时,将铀氧化物再循环至 所述第二区域产生具有较低氟化物含量和氧与铀比率的铀氧化物,并且其中所述具有不可接受的高氟含量的铀氧化物被供给到该第一区域 在没有任何进料UF6或蒸汽的情况下,并且由输送装置直接输送到容器的第二区域中。