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Human Factors, Instrumentation & Controls
Improving task performance, system reliability, system and personnel safety, efficiency, and effectiveness are the division's main objectives. Its major areas of interest include task design, procedures, training, instrument and control layout and placement, stress control, anthropometrics, psychological input, and motivation.
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2025 ANS Annual Conference
June 15–18, 2025
Chicago, IL|Chicago Marriott Downtown
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Smarter waste strategies: Helping deliver on the promise of advanced nuclear
At COP28, held in Dubai in 2023, a clear consensus emerged: Nuclear energy must be a cornerstone of the global clean energy transition. With electricity demand projected to soar as we decarbonize not just power but also industry, transport, and heat, the case for new nuclear is compelling. More than 20 countries committed to tripling global nuclear capacity by 2050. In the United States alone, the Department of Energy forecasts that the country’s current nuclear capacity could more than triple, adding 200 GW of new nuclear to the existing 95 GW by mid-century.
Constantinos Syros,* Claudio Ronchi, Cinzia Spanó
Nuclear Technology | Volume 94 | Number 2 | May 1991 | Pages 213-227
Technical Paper | Advances in Reactor Accident Consequence Assessment / Nuclear Reactor Safety | doi.org/10.13182/NT91-A34543
Articles are hosted by Taylor and Francis Online.
A semianalytical nonlinear model is described for the calculation of the burst release and release rate of volatile fission product (VFP) from a fuel pellet under steady-state and transient reactor conditions as well as the radial density distribution in the open porosity. The density of the VFP in the porosity channels is assumed to be c(r, t) = φ(r)exp[—LT(r)ω(t)] + Λ-1(t), where L is an analytical function of parameters characterizing the physics and the geometry of the pellet; φ(r) rigorously satisfies the required boundary conditions; and ω(t), the solution of a highly nonlinear differential equation, is a time function (“kinetic time”) that represents the evolution of the density profile. The constant Λ is suitably calculated with the zeroes of the Bessel function Jo(x). The density c(r, t) of the VFP in the open porosity of the pellet is used to find the pressure p(r, t) in the open pores. The integration procedure of the transport equation for different initial and boundary conditions is described. Calculation experiments are presented and discussed.