Study on highly-efficient enrichment of tritium water by use of distillation column packed with hydrophilic adsorbent

亲水吸附剂精馏塔高效富集氚水的研究

基本信息

  • 批准号:
    17360443
  • 负责人:
  • 金额:
    $ 5.47万
  • 依托单位:
  • 依托单位国家:
    日本
  • 项目类别:
    Grant-in-Aid for Scientific Research (B)
  • 财政年份:
    2005
  • 资助国家:
    日本
  • 起止时间:
    2005 至 2007
  • 项目状态:
    已结题

项目摘要

Tritium-waste water will be drained from facilities for a tritium fuel cycle of a future fusion reactor or is presently exhausted from uranium fuel reprocessing plant for a fission reactor. When its concentration is lower than the legally regulated one (60Bq/cm^3), it can be drained from the facilities as it is. When it is higher than the legal value, the drain water has to be diluted by a large amount of fresh water or has to be enriched/separated in the facilities. There is less difficulty in the dilution process. However, when its tritium concentration is much higher than the regulated level, we need to develop a new isotope separation system to decontaminate the tritium-waste water drain at a lower level than the regulated level and to separate a small amount of high-level tritium water. Although the H_2H_2O isotopic exchange method that was used for a heavy water separation of CANDU reactor can be applied to the tritium enrichment, the facilities for the deuterium separation are h … More uge, and they need a special and expensive Pt catalyst. In addition, the Pt catalyst performance is deteriorated by CO that will be included in the exhaust gas of fusion facilities. Therefore, the process needs pretreatment to reduce some pollutants. In the present study, a new isotope separation method to enhance the performance of a classical distillation column with use of hydrophilic adsorbents. As candidates for the hydrophilic adsorbent, silica-gel and zeolite adsorbents were comparatively experimented in the present study. The original isotope separation factor based on the difference in vapor pressure between H_2O and HTO is 1.028. It was found that the isotope separation factor was enhanced to 1.1 to 1.2 with the use of the hydrophilic adsorbent, and therefore it can downsize the scale of the tritium enrichment and separation. The silica-gel column attained the comparatively large separation performance in the various ranges of vapor flow rate. On the other hand, the zeolite column (commercial name Linde molecular sieve 13X) attained the largest isotope separation performance at very small vapor flow rate, but the separation factor decreased at higher flow rate. This is because the exchange reaction between HTO in the vapor phase and H_2O on the adsorbent is comparatively slow. Therefore, the number of transfer unit (NTP) of the zeolite column was much smaller than that of the silica-gel column. The zeolite column is considered to be effective especially for the very small vapor flow rate. The transient tritium enrichment performance was experimentally determined, and it was found that the numerical calculation based on the plate model that uses the number of transfer unit fitted the experimental ones. The experimental and numerical results were presented in the research papers listed in the next page. The abstract of the present scientific research is summarized in a report. Less
氚废水将从未来聚变反应堆的氚燃料循环设施中排出,或目前从裂变反应堆的铀燃料后处理工厂中排出。当其浓度低于法定浓度(60Bq/cm^3)时,可将其原样排出设施。当浓度高于法定值时,排放的水必须用大量的淡水稀释或在设施中进行浓缩/分离。在稀释过程中困难较少。然而,当其氚浓度远高于规定水平时,我们需要开发一种新的同位素分离系统,在低于规定水平的氚废水排水口进行净化,并分离少量高氚水。用于CANDU反应堆重水分离的H_2H_2O同位素交换法虽然可以应用于氚富集,但分离氘的设施体积较大,且需要特殊且昂贵的Pt催化剂。此外,熔合设备废气中含有的CO会使Pt催化剂的性能恶化。因此,该工艺需要预处理,以减少一些污染物。本文研究了一种利用亲水吸附剂提高经典精馏塔分离性能的同位素分离新方法。作为亲水吸附剂的候选材料,本文对硅胶和沸石吸附剂进行了比较实验。基于H_2O和HTO蒸气压差的原始同位素分离因子为1.028。结果表明,亲水吸附剂可将同位素分离系数提高到1.1 ~ 1.2,从而减小了氚富集分离的规模。硅胶柱在不同汽流量范围内均具有较好的分离性能。另一方面,沸石柱(商品名林德分子筛13X)在极小蒸汽流量下的同位素分离性能最大,但在较大流量下分离系数降低。这是因为气相中的HTO与吸附剂上的H_2O之间的交换反应比较缓慢。因此,沸石柱的转移单元数(NTP)远小于硅胶柱。沸石柱被认为是有效的,特别是对于非常小的蒸汽流量。对氚的瞬态富集性能进行了实验测定,发现采用迁移单元数的平板模型的数值计算与实验结果吻合。实验和数值结果在下一页列出的研究论文中给出。目前的科学研究摘要在一份报告中进行了总结。少

项目成果

期刊论文数量(0)
专著数量(0)
科研奖励数量(0)
会议论文数量(0)
专利数量(0)
Study on water uptake of proton exchange membrane by using tritiated water sorption method
  • DOI:
    10.1016/j.ijhydene.2005.02.006
  • 发表时间:
    2005-08
  • 期刊:
  • 影响因子:
    7.2
  • 作者:
    H. Takata;M. Nishikawa;Yusaku Arimura;T. Egawa;S. Fukada;M. Yoshitake
  • 通讯作者:
    H. Takata;M. Nishikawa;Yusaku Arimura;T. Egawa;S. Fukada;M. Yoshitake
Tritium recovery system for Li-Pb loop of inertial fusion reactor
惯性聚变反应堆Li-Pb回路氚回收系统
Tritium recovery system for Li-Pb loop of inerfial fusion reactor
惯性聚变反应堆Li-Pb回路氚回收系统
国際核融合材料照射施設(IFMIF)の設計と開発の現状 3.ターゲット系の開発
国际聚变材料辐照装置(IFMIF)的设计和开发现状 3.靶系统的开发
Concentration profiles of tritium penetrated in concrete
渗入混凝土中的氚浓度分布
  • DOI:
  • 发表时间:
    2008
  • 期刊:
  • 影响因子:
    0.9
  • 作者:
    H.Takata;K.Furuichi;M.Nishikawa;S.Fukada;K.Katayama;T.Takeishi;K.Kobayashi;T.Hayashi;H.Namba
  • 通讯作者:
    H.Namba
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FUKADA Satoshi其他文献

FUKADA Satoshi的其他文献

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{{ truncateString('FUKADA Satoshi', 18)}}的其他基金

Study on hydrogen production system assisted with heat pumps andhigh-temperature gas-cooled reactor
热泵辅助高温气冷堆制氢系统研究
  • 批准号:
    22656212
  • 财政年份:
    2010
  • 资助金额:
    $ 5.47万
  • 项目类别:
    Grant-in-Aid for Challenging Exploratory Research
Clarification of tritium transfer inside concrete bui! di ng of fusion reactor and development of technology to decrease tritium permeation through concrete walIs
混凝土建筑内氚转移的澄清!
  • 批准号:
    21360451
  • 财政年份:
    2009
  • 资助金额:
    $ 5.47万
  • 项目类别:
    Grant-in-Aid for Scientific Research (B)
Advanced study of tritium recovery from molten salt Flibe blanket in fusion reactor
聚变反应堆熔盐Flibe包层回收氚的最新研究
  • 批准号:
    14380220
  • 财政年份:
    2002
  • 资助金额:
    $ 5.47万
  • 项目类别:
    Grant-in-Aid for Scientific Research (B)
A study on enrichment and volume reduction of tritiated water in a fusion reactor using photocatalysis
聚变反应堆中氚化水光催化富集减容研究
  • 批准号:
    12680493
  • 财政年份:
    2000
  • 资助金额:
    $ 5.47万
  • 项目类别:
    Grant-in-Aid for Scientific Research (C)
Study of multi-column cold trap with highly effective recovery rate of tritium water vapor
高效氚水蒸气回收率的多柱冷阱研究
  • 批准号:
    11558058
  • 财政年份:
    1999
  • 资助金额:
    $ 5.47万
  • 项目类别:
    Grant-in-Aid for Scientific Research (B).
A study of surface pretreatment of tritium-getter alloy for enhancement of insensitiveness to impurities
氚吸气合金表面预处理增强杂质不敏感性的研究
  • 批准号:
    10680473
  • 财政年份:
    1998
  • 资助金额:
    $ 5.47万
  • 项目类别:
    Grant-in-Aid for Scientific Research (C)
Gas separation by a Pd-plated alumina membrane for a small-scale emergency atmospheric detritiation system
小型应急大气除氚系统的镀钯氧化铝膜气体分离
  • 批准号:
    07808056
  • 财政年份:
    1995
  • 资助金额:
    $ 5.47万
  • 项目类别:
    Grant-in-Aid for Scientific Research (C)

相似海外基金

Synthesizing Optimal Batch Distillation Column Configuration
综合最佳间歇蒸馏塔配置
  • 批准号:
    9729074
  • 财政年份:
    1998
  • 资助金额:
    $ 5.47万
  • 项目类别:
    Standard Grant
Coupled Chemical Reactor/Distillation Column Experiment for Chemical Engineering Majors
化工专业化学反应器/精馏塔耦合实验
  • 批准号:
    9251715
  • 财政年份:
    1992
  • 资助金额:
    $ 5.47万
  • 项目类别:
    Standard Grant
Study on Start-up Operation of Distillation Column Using Artificial Intelligence
利用人工智能进行精馏塔启动操作的研究
  • 批准号:
    62550698
  • 财政年份:
    1987
  • 资助金额:
    $ 5.47万
  • 项目类别:
    Grant-in-Aid for General Scientific Research (C)
Acquistion of a Computer Controlled Distillation Column
购置计算机控制蒸馏塔
  • 批准号:
    7811097
  • 财政年份:
    1978
  • 资助金额:
    $ 5.47万
  • 项目类别:
    Standard Grant
Distillation Column Pressure Control By Hot-Vapor Bypassing
通过热蒸汽旁路控制蒸馏塔压力
  • 批准号:
    7621420
  • 财政年份:
    1977
  • 资助金额:
    $ 5.47万
  • 项目类别:
    Standard Grant
Experimental Transient Response of a Pilot-Plant Distillation Column
中试蒸馏塔的实验瞬态响应
  • 批准号:
    6216248
  • 财政年份:
    1962
  • 资助金额:
    $ 5.47万
  • 项目类别:
Transient Response Characteristics of Distillation Column;
精馏塔的瞬态响应特性;
  • 批准号:
    5905018
  • 财政年份:
    1959
  • 资助金额:
    $ 5.47万
  • 项目类别:
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