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• W2015767462 abstract "In practice, raffinate generated from a nuclear facility is either neutralized or evaporated or diluted and dispersed. Value recovery from such lean raffinate streams (≈0.6 g/l U+6) is of immense importance in view of the potential uranium resource. The HFDLM technique was found to be quite stable and promising for the complete recovery of uranium from plant raffinate. A model was developed for simulating transport phenomena of U from the given raffinate. Here, the developed model is extended to address the large-scale application of HF contactors. Mass transfer coefficients evaluated from the module of 1.4 m2 area have been utilized to predict the performance of the module of 8.1 m2 area. Successful large-scale tests were accomplished by employing a bigger membrane contactor with 8.1 m2 membrane area. Large scale set up has a throughput of 51 l/hr for raffinate taken. The overall mass transfer coefficient of a system of 3 contactors of 1.4 m2 area combined in series is obtained as 1.55 × 10−2 cm/s; stage efficiency of each contactor is found as 60%. A flux of 9.2 × 10−3 moles/m2/hr was obtained for uranium which is about 3–4 times of supported liquid membrane in the HF module and about 10–50 times of solvent extraction in the conventional contactor." @default.
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• W2015767462 date "2013-11-02" @default.
• W2015767462 modified "2023-09-23" @default.
• W2015767462 title "A Mathematical Model for Size and Number Scale Up of Hollow Fiber Modules for the Recovery of Uranium from Acidic Nuclear Waste using the DLM Technique" @default.
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• W2015767462 doi "https://doi.org/10.1080/01496395.2013.807825" @default.
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