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

机译:NIFS中CECE工艺氢同位素分离的现状

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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:在全国融合科学研究所,已经进行了通过组合电解催化交换(CECE)处理的氢异形络合物分离,以便将其应用于水脱模系统的大螺旋装置(LHD)的DD燃烧实验系统。氢气和氘的同位素分离实验用两种填充有咯咯醇催化剂的填充床(4.0-6.7mm球形,0.8wt%Pt沉积)和德克逊纱布环(6mm外径,6mm高度)。一个是层叠床,其中kogel催化剂层和迪克森纱布环的层交替填充。另一个是均匀的床,其中kogel催化剂和dixon纱布环混合并均匀地填充在柱中。均匀床的分散性能明显大于层状床的分散性能,其中催化剂的量相等。均匀的包装床表现出精细的表现;压降在40-300帕/ m的范围是小的和汽 - 液传质系数变得大于900千摩尔/米〜3 /小时,而表面速度范围为0.2-0.7米/秒。

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