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L. A. But V. D. Vdovichenko O. B. Gromov A. N. Evdokimov A. V. Ivanov I. A. Logvinenko P. I. Mikheev D. V. Fedorova V. V. Shilov 《Theoretical Foundations of Chemical Engineering》2016,50(5):884-889
The mechanism of uranium tetrafluoride formation during the reduction of depleted uranium hexafluoride in hydrogen fluoride flame has been studied. Based on the performed studies, it has been established that powder uranium tetrafluoride with characteristics that enable it to be used for both long-term storage (minimum specific surface area, 0.6 ± 0.1 m2/g; untapped density, 2.7 g/cm3) and metallic uranium production (maximum specific surface area, 1.45 m2/g) can be obtained by adjusting the operational regime of a flame reactor. 相似文献
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Reduction, followed by hydrofluorination of uranium trioxide UO3 to produce uranium tetrafluoride UF4 is one of the stages of the French nuclear fuel making route. This dual operation is carried out in a specific reactor known as a moving bed furnace, consisting of a series of steel cylinders that form an L. In this first part of a two-part paper, the mathematical modelling of the furnace is presented in detail. The model describes solid and gas flow, heat transfer by convection, conduction and radiation in the moving bed and in the walls of the furnace, and chemical reactions. In the vertical part of the reactor, mass, momentum and energy balances are solved using the finite volume method. The horizontal part is modelled by a cascade of stirred gas and solid reactors. The assumptions and equations of the model, as well as the boundary conditions and numerical solution techniques are detailed. An example of calculated results is presented and found to agree satisfactorily with available measurements. Application of the model is discussed in Part 2. 相似文献
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The corrosion mechanism and microstructural characteristics of yttria (Y2 O3 ) exposed to uranium hexafluoride (UF4 ) and uranium tetrafluoride gases at temperatures above 900°C were investigated. Processed yttria samples were exposed for times ranging from 5 to 40 min. A weight increase was observed after each test exposure. An outer corrosion scale composed of UO2 and YF3 , and an inner corrosion layer of YF3 , were observed following the UF6 reaction at nearly 1200 K. During the UF4 exposure, an outer layer containing a liquid mixture of fluoride, oxygen, yttrium, uranium compounds, a secondary reaction layer of UO2 followed by an inner layer composed of a solution of Y2 O3 and YF3 , possibly in the form of YOF inner layer, were observed. It was found that the corrosion process is controlled by the diffusion which is evidenced by the parabolic growth rate of the secondary layer. After completion of the solidification process, the formation of a eutectic region and dendrites were observed throughout the outer scale. In general, at temperatures above 1173 K, high corrosion rates were observed, and yttria did not appear to be a viable containment material for UF4 and UF6 . 相似文献
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The French nuclear fuel making route uses, prior to enrichment, uranium tetrafluoride UF4 obtained from the reduction, followed by hydrofluorination of uranium trioxide UO3. These two steps are carried out in a specific reactor known as a moving bed furnace. We developed a steady-state numerical model of the moving bed furnace, described in Part 1. In the Part 2, calculation results for a reference set of operating parameters of the furnace are presented in term of temperature, reaction rates, solid and gas compositions. Results analysis enlightens the detail of the furnace behaviour in its different zones. Unknown features have been revealed, such as thermodynamic limitation of the hydrofluorination reaction in the hot core of the moving bed. A sensibility study of various operating parameters shows how some can influence the UF4 quality and underlines the strong coupling between the different zones of the furnace. Finally, the model is applied to define an optimal temperature progression in the furnace and suggests geometrical modifications. Besides, the validity of using the law of additive reaction times for calculating the reaction rates in such a reactor model has been checked for the first time against a numerical grain model. 相似文献
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于剑昆 《化学推进剂与高分子材料》2004,2(5):10-13
(接第3期第17页 )2.2.1 吸附法意大利一家公司的专利介绍一种用特制的合金脱除全氟烷中水分和氧的方法[36]。该合金组成质量分数为Zr47%~70%,V24%~45%,Fe5%~10%,将其加工成直径<125靘的粒子,在真空或惰性气体保护下于300℃处理全氟烷,可有效去除水分和氧。杜邦公司的专利介绍一种使含空气和CO的全氟烷与MnO2和CuO混合粒子接触,在高温下使CO氧化为CO2;再用蛭石承载的碱石灰或NaOH粒子吸收CO2,最后用4A分子筛干燥提纯全氟烷的工艺[37]。催化剂粒子通常为8~24目,质量分数为MnO267%~86%、CuO14%~33%,反应温度200℃。该方法可连续进行… 相似文献
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Yasutake Ohishi Shigeki Sakaguchi Shiro Takahashi 《Journal of the American Ceramic Society》1987,70(4):81-C-
The glass containing reduced zirconium exhibits a photoemission band at 480 nm and an excitation band from 230 to 370 nm. Reduced zirconium tetrafluoride has broad absorption at 400 nm. Reduction of zirconium tetrafluoride occurs through fluorine or oxygen impurity elimination. When fluorine ion deficiency occurs, emission and excitation bands appear at 440 and 350 nm, respectively. When oxygen deficiency occurs, emission and excitation bands appear at 480 and 300 nm, respectively. 相似文献
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A new model has been developed to analyze the performance of a moving bed reactor producing uranium tetrafluoride. The model includes the solid and gas flow rates, heat transfer by convection, conduction and radiation between gas and solid streams and by the external surrounding. A kinetics model has been also developed for the gas–solid reactions on the basis of the grain model in which, the different resistances are taken into account to determine the overall reaction rates. This study provides an initial and theoretical basis for optimum design of the moving bed on the basis of the kinetics models. The optimum design is carried out from the viewpoint of required length of the reactor and the maximum conversion. According to the primary expectations which are provided by the kinetics models, the feed temperature seems not to have any effective influence on the reactor performance. On the other hand, it is predicted that the inlet gas flow rate contributes an important role. The investigations show that although the kinetics models are rather useful in primary estimations, the strong interdependence between different zones of the reactor may prevent general expressions. 相似文献
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电解法制得的氟气含有氮气、氟化氢和四氟化碳等杂质。利用氯化钠与氟气反应生成氯气,经NaOH溶液吸收氯气后用普通的气相色谱测定其中四氟化碳含量,操作简单、快速。 相似文献
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采用配有放电离子化检测器的气相色谱仪分析高纯四氟化碳中痕量气体杂质。研究了分析四氟化碳中氧气、氮气、一氧化碳、二氧化碳和六氟化硫等气体杂质的操作参数,确定了高纯四氟化碳中痕量气体杂质的分析方法。 相似文献
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磷肥副产物氟硅酸钠热解可制备四氟化硅气体,该方法无废弃物产生,生产成本较低,具有广阔的发展前景。对影响氟硅酸钠热解的各种因素进行了一系列静态实验研究,实验发现,氟硅酸钠热解的最佳反应温度应保持在中温区(500~700 ℃),反应压力维持在常压或微负压状态。利用该法生产四氟化硅气体具有气体纯度高和无副产物产生的特点。 相似文献
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以L-丙氨酸和四氟化硫为原料,压力下经一步氟化反应制得α-三氟甲基乙胺。实验研究获得的最佳工艺条件为:以100 g L-丙氨酸为原料,n(L-丙氨酸)∶n(四氟化硫)为1∶2,55℃及18-19 kgf/cm^2压力下保温反应12 h,产品收率在55%以上,产品盐酸盐熔点在218.5℃以上。 相似文献
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普钙含氟废气的回收利用 总被引:1,自引:0,他引:1
普钙生产中废气的主要成分是SiF4 。若直接排入大气 ,将严重污染环境。为治理含氟废气 ,沿用已久的方法是处理成Na2 SiF6,本文提出的方法是处理成MgSiF6,同时也有精碘制成。 相似文献