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Present status of hydrogen isotope separation by CECE process at the NIFS

机译:NIFS通过CECE工艺分离氢同位素的现状

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At the National Institute for Fusion Science experimental studies on hydrogen isotope separation by a combined electrolysis catalytic exchange (CECE) process have been carried out in order to apply it to the system of water detritiation for D-D burning experiments of the large helical device (LHD). Isotope separation experiments of hydrogen and deuterium are performed with two types of packed beds filled with Kogel catalysts (4.0-6.7 mm spherical, 0.8 wt% Pt deposited) and Dixon gauze rings (6 mm outer diameter, 6 mm height). One is the layered bed where layers of Kogel catalysts and that of Dixon gauze rings are filled in the column alternately. The other is the homogeneous bed where Kogel catalysts and Dixon gauze rings are mixed and filled in the column homogeneously. The separative performance of the homogeneous bed is appreciably greater than that of the layered bed, where the quantities of the catalysts are equal for both beds. The homogeneous packed bed exhibits fine performances; pressure drop is small in the range of 40-300 Pa/m and the coefficient of vapor-liquid mass transfer becomes more than 900 kmol/m~3/h, while the superficial velocity is in the range 0.2-0.7 m/s.
机译:在美国国家融合科学研究院,已经进行了通过组合电解催化交换(CECE)分离氢同位素的实验研究,以便将其应用于大型螺旋装置(LHD)DD燃烧实验的水处理系统中。氢和氘的同位素分离实验是用填充有Kogel催化剂(4.0-6.7毫米球形,沉积0.8 wt%Pt)和Dixon纱网环(外径6 mm,高度6 mm)的两种填充床进行的。一种是层状床,其中在塔中交替填充Kogel催化剂层和Dixon纱环。另一个是均相床,其中将Kogel催化剂和Dixon纱网环混合并均匀地填充到色谱柱中。均相床的分离性能明显大于层状床的分离性能,其中两层床的催化剂量相等。均匀填充床表现出良好的性能;压降在40-300 Pa / m范围内较小,气液传质系数大于900 kmol / m〜3 / h,而表观速度在0.2-0.7 m / s范围内。

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