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- W52991736 abstract "Experiments have confirmed the validity of a novel design for a nitric acid concentration system for use in shielded nuclear fuel reprocessing plants. Current plans for producing the scrub solution for the IODOX process require the concentration and recycle of low strength (< 68.5 wt %) nitric acid sources. The described system utilizes extractive distillation with Mg(NO/sub 3/)/sub 2/ as the solvent and features two pots: an extractive distillation pot in which a concentrated acid product is obtained by contacting the acid feed with the solvent and a solvent recovery pot in which the solvent is dehydrated and recovered for recycle. In these experiments, a concentrated product of 89 wt % nitric acid was produced from azeotropic feed. The available vapor-liquid equilibria data for the Mg(NO/sub 3/)/sub 2/-HNO/sub 3/-H/sub 2/O system has been empirically correlated, and a design methodology has been developed for the two-pot extractive distillation process." @default.
- W52991736 created "2016-06-24" @default.
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- W52991736 date "1982-12-01" @default.
- W52991736 modified "2023-10-14" @default.
- W52991736 title "Extractive distillation of nitric acid using the two-pot concept" @default.
- W52991736 doi "https://doi.org/10.2172/6900391" @default.
- W52991736 hasPublicationYear "1982" @default.
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