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- W54399995 abstract "Studies were made of the process characteristics of a plant to decontaminate tritiated water using dual temperature exchange with VH/sub 2/. Feed to the plant consists of 300 kg/day on water containing 1 Ci/kg of tritium. A reference design was developed based on a decontamination factor of 10/sup 2/ and 10 kg/day of enriched product. This design requires a total of 48 ideal separation stages, 22 stages in the enriching section and 26 stages in the stripping section. Only low grade heat is required for the heating cycle and a relatively small (12 ton) ice machine is required for the cooling cycle. A total plant inventory of approximately 10 tons VH/sub 2/ is required. A mechanical design of the dual temperature stage complete with all heat transfer surfaces and flow diverters was devised and modeled. Since the process involves periodic swings in temperature between 0 and 60/sup 0/C, a substantial portion of the operation is expected to be in unsteady state transition from one state to another. A two-step experimental program has been presented: the first step consists of a single stage unit, i.e., one hot bed and one cold bed operating in a simple closed loop. The second stagemore » in the experimental program would consist of five stages operating as a small cascade. (DLC)« less" @default.
- W54399995 created "2016-06-24" @default.
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- W54399995 date "1976-01-22" @default.
- W54399995 modified "2023-09-23" @default.
- W54399995 title "Report on process design studies of a tritium recovery process using dual temperature exchange with metal hydrides" @default.
- W54399995 doi "https://doi.org/10.2172/7341328" @default.
- W54399995 hasPublicationYear "1976" @default.
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