The Optimal Equilibrium Approaches in a GS Plant for Deuterium Separation

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Influence of equilibrium approach as design parameter in GS plant based on H<SUB>2</SUB>S-H<SUB>2</SUB>O isotopic exchange for heavy water production is studied. The results obtained by modelling and the optimum finding are shown for a plant with a single cold feeding and with two hot-cold feedings. The optimum equilibrium approach for a minimum plant volume is obtained at a value of 98.2% and for a minimum specific cost of heavy water at 98.5%. For a plant with two feedings and optimum design and operation, the equilibrium approach at the top of first and second stage cold towers are both about 98.5% and that of the hot tower is about 97.3%.

収録刊行物

  • Journal of nuclear science and technology

    Journal of nuclear science and technology 32(9), 921-927, 1995-09-25

    Atomic Energy Society of Japan

参考文献:  8件中 1-8件 を表示

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各種コード

  • NII論文ID(NAID)
    10002073223
  • NII書誌ID(NCID)
    AA00703720
  • 本文言語コード
    ENG
  • 資料種別
    ART
  • ISSN
    00223131
  • データ提供元
    CJP書誌  J-STAGE 
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