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Division Spotlight
Thermal Hydraulics
The division provides a forum for focused technical dialogue on thermal hydraulic technology in the nuclear industry. Specifically, this will include heat transfer and fluid mechanics involved in the utilization of nuclear energy. It is intended to attract the highest quality of theoretical and experimental work to ANS, including research on basic phenomena and application to nuclear system design.
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ANS Student Conference 2025
April 3–5, 2025
Albuquerque, NM|The University of New Mexico
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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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Latest News
Norway’s Halden reactor takes first step toward decommissioning
The government of Norway has granted the transfer of the Halden research reactor from the Institute for Energy Technology (IFE) to the state agency Norwegian Nuclear Decommissioning (NND). The 25-MWt Halden boiling water reactor operated from 1958 to 2018 and was used in the research of nuclear fuel, reactor internals, plant procedures and monitoring, and human factors.
O. E. Dwyer
Nuclear Science and Engineering | Volume 21 | Number 1 | January 1965 | Pages 79-89
Technical Paper | doi.org/10.13182/NSE65-A21017
Articles are hosted by Taylor and Francis Online.
An analytical study has been made of the general problem of heat-transfer to liquid metals flowing between parallel plates. All the results are for the conditions of uniform heat fluxes and fully-established temperature and velocity profiles. Both unilateral and bilateral heat-transfer situations have been considered. In the former, three different methods of determining the velocity profiles were compared; and for each of these, three different types of profile curves for the eddy diffusivity of momentum, ∈M, were compared. The three different methods of determining the velocity profiles showed remarkably good agreement. In the case of bilateral heat transfer, the fraction of total heat transfer to the fluid from any one plate, ξ, was varied from zero to unity. It was found that the heat-transfer coefficient for any one plate is a sensitive function of ξ for that plate. Above ξ = 0.31, the coefficients are positive; below it, they are negative. At ξ = 0.31, the coefficient is infinite, because at this condition the difference between wall and bulk temperatures is zero. As ξ approaches 0.50, from either above or below, the shape of the εM profile in the vicinity of the center of the channel has less and less effect on the heat-transfer coefficient. When ξ = 0.50, the effect is negligible for all practical purposes. There are no adequate experimental data available with which to test the calculated Nusselt numbers, but indications are that the recommended relationships are reasonably correct.