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Campbell, M.H.; Frame, J.M.; Dudey, N.D.; Kiel, G.R.; Mesec, V.; Woodfield, F.W.; Binney, S.E.; Jante, M.R.; Anderson, R.C.; Clark, G.T.
Bendix Field Engineering Corp., Grand Junction, CO (USA); Exxon Nuclear Co., Inc., Richland, WA (USA); Oregon State Univ., Corvallis (USA). Dept. of Nuclear Engineering; Vitro Engineering Co., New York (USA)1979
Bendix Field Engineering Corp., Grand Junction, CO (USA); Exxon Nuclear Co., Inc., Richland, WA (USA); Oregon State Univ., Corvallis (USA). Dept. of Nuclear Engineering; Vitro Engineering Co., New York (USA)1979
AbstractAbstract
[en] A major assessment was made of the uranium resources in seawater. Several concepts for moving seawater to recover the uranium were investigated, including pumping the seawater and using natural ocean currents or tides directly. The optimal site chosen was on the southeastern Puerto Rico coast, with the south U.S. Atlantic coast as an alternate. The various processes for extracting uranium from seawater were reviewed, with the adsorption process being the most promising at the present time. Of the possible adsorbents, hydrous titanium oxide was found to have the best properties. A uranium extraction plant was conceptually designed. Of the possible methods for contacting the seawater with the adsorbent, a continuous fluidized bed concept was chosen as most practical for a pumped system. A plant recovering 500 tonnes of U3O8 per year requires 5900 cubic meters per second of seawater to be pumped through the adsorbent beds for a 70% overall recovery efficiency. Total cost of the plant was estimated to be about $6.2 billion. A computer model for the process was used for parametric sensitivity studies and economic projections. Several design case variations were developed. Other topics addressed were the impact of co-product recovery, environmental considerations, etc
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Feb 1979; 169 p; OSU-NE--7901(VOL.1); Available from NTIS., PC A08/MF A01
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