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U.S. Department of Energy
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AEC RESEARCH AND DEVELOPMENT QUARTERLY REPORT FOR APRIL, MAY, AND JUNE 1957

Technical Report ·
OSTI ID:4328758

Phase I is concerned with the separation of boron isotopes 10 and 11. The presently used method of separation of boron isotopes is that of an association-dissociation reaction employing the dimethyl ether-boron trifluoride complex. In that the BF/sub 3/ containing B/sup 10/ associates with dimethyl ether at a slightly greater rate than BF/sub 3/ containing the B/sup 11/ isotope, the liquid phase becomes enriched in B/sup 10/ and the vapor phase becomes enriched in B/sup 11/. The reaction is carried out in extremely effective continuous fractionation columns, the B/sup 10/ enriched complex being recovered from the bottoms. A second method for the separation of boron isotopes is in the development stage. This method involves an association-dissociation process using an anisole-boron trifluoride complex. The method is dependent on an exchange between BF/sub 3/ gas and anisoleboron trifiuoride liquid complex. The desired boron-10 isotope is concentrated in the liquid phase. The boron isotope separation factor is greater for the anisole-BF/sub 3/ complex system than for the dimethyl ether-BF/sub 3/ system. Increased production of B/sup 10/ or new construction would be expected to profit from the successful development of the anisole-BF/sub 3/ system. Phase II is concerned with the reduction of boron compounds (product of Phase I) to the elemental form. Although hydrogen reduction of boron trichloride using a hot wire was used in plant operations, fused salt electrolysis is used at present. The process involves the electrolysis of potassium fluoroborate in a potassium chloride melt. Research work is primarily directed at increasing the recovery of boron. (auth)

Research Organization:
Hooker Electrochemical Co., Niagara Falls, N.Y.
NSA Number:
NSA-12-001288
OSTI ID:
4328758
Report Number(s):
HEC-79
Country of Publication:
United States
Language:
English

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