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Division Spotlight
Accelerator Applications
The division was organized to promote the advancement of knowledge of the use of particle accelerator technologies for nuclear and other applications. It focuses on production of neutrons and other particles, utilization of these particles for scientific or industrial purposes, such as the production or destruction of radionuclides significant to energy, medicine, defense or other endeavors, as well as imaging and diagnostics.
Meeting Spotlight
ANS Student Conference 2025
April 3–5, 2025
Albuquerque, NM|The University of New Mexico
Standards Program
The Standards Committee is responsible for the development and maintenance of voluntary consensus standards that address the design, analysis, and operation of components, systems, and facilities related to the application of nuclear science and technology. Find out What’s New, check out the Standards Store, or Get Involved today!
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Molten salt research is focus of ANS local section presentation
The American Nuclear Society’s Chicago–Great Lakes Local Section hosted a presentation on February 27 on developments at the molten salt research reactor at Abilene Christian University’s Nuclear Energy Experimental Testing (NEXT) Lab.
A recording of the presentation is available on the ANS website.
Donald R. Olander, Manson Benedict
Nuclear Science and Engineering | Volume 14 | Number 3 | November 1962 | Pages 287-294
doi.org/10.13182/NSE62-A26218
Articles are hosted by Taylor and Francis Online.
The mechanism of water extraction into tributyl phosphate—n-hexane solvents has been investigated in a stirred-vessel transfer cell. The effects of stirrer speed, temperature, and the comparison of the TBP-hexane results to those for water transfer into ordinary nonreacting organic solvents strongly suggest that the process is one of simple mass transfer. No effect of complexing, which might have formed the species H20-TBP, was found. The kinetic data (in the form of a single-phase mass transfer coefficient) were all correlated to within ± 10% by the relation where k is the individual mass transfer coefficient, v the kinematic viscosity of the solvent phase, ω the stirrer speed, and Sc the Schmidt number, v/D.