The Optimal Equilibrium Approaches in a GS Plant for Deuterium Separation.

• PAVELESCU Marian

  Institute of Cryogenics and Isotopic Separations

抄録

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%.

収録刊行物

• Ｊｏｕｒｎａｌ　ｏｆ　Ｎｕｃｌｅａｒ　Ｓｃｉｅｎｃｅ　ａｎｄ　Ｔｅｃｈｎｏｌｏｇｙ（日本原子力学会英文論文誌）

  Ｊｏｕｒｎａｌ　ｏｆ　Ｎｕｃｌｅａｒ　Ｓｃｉｅｎｃｅ　ａｎｄ　Ｔｅｃｈｎｏｌｏｇｙ（日本原子力学会英文論文誌） 32 (9), 921-927, 1995

  一般社団法人 日本原子力学会

キーワード

• heavy water
• heavy water plants
• GS plant
• design parameter
• equilibrium
• optimization
• hydrogen sulfide
• water
• isotopic exchange
• feeding
• operating cost
• design

詳細情報

• CRID: 1390001204093695360
• NII論文ID: 10002073223
• NII書誌ID: AA00703720
• DOI: 10.3327/jnst.32.921
• COI: 1:CAS:528:DyaK2MXoslyhu78%3D
• ISSN: 18811248
• ISSN: 00223131
• 本文言語コード: en
• データソース種別:
  • JaLC
  • Crossref
  • CiNii Articles
• 抄録ライセンスフラグ: 使用不可