The Optimal Equilibrium Approaches in a GS Plant for Deuterium Separation.
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- PAVELESCU Marian
- Institute of Cryogenics and Isotopic Separations
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Abstract
Influence of equilibrium approach as design parameter in GS plant based on H2S-H2O 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%.
Journal
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- Journal of Nuclear Science and Technology
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Journal of Nuclear Science and Technology 32 (9), 921-927, 1995
Atomic Energy Society of Japan
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Details 詳細情報について
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- CRID
- 1390001204093695360
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- NII Article ID
- 10002073223
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- NII Book ID
- AA00703720
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- COI
- 1:CAS:528:DyaK2MXoslyhu78%3D
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- ISSN
- 18811248
- 00223131
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- Text Lang
- en
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- Data Source
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- JaLC
- Crossref
- CiNii Articles
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- Abstract License Flag
- Disallowed