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RIC panel discusses pathway to fusion commercialization
Fusion leaders at the Nuclear Regulatory Commission’s annual Regulatory Information Conference discussed the path forward for regulating the burgeoning fusion industry. The speakers discussed government and private industry initiatives in the United States and United Kingdom, with a focus on efforts shaping the near-term deployment of commercial fusion machines.
A recurring theme was the need to explain the difference between fission and fusion. Representatives from the Department of Energy and Type One Energy highlighted this as an important distinction for regulators, as it will allow fusion to undergo its own independent maturation process for developing standards and regulations in the same way that fission has. Lea Perlas, Fusion Program director at the Virginia Department of Health, said that confusion between fission and fusion has been a common cause for misplaced concerns among community members surrounding Commonwealth Fusion Systems’ proposed fusion plant site near Richmond, Va.
Daniel William Tedder, Bruce C. Finney
Nuclear Technology | Volume 133 | Number 2 | February 2001 | Pages 242-252
Technical Paper | Radioactive Waste Management and Disposal | doi.org/10.13182/NT01-A3172
Articles are hosted by Taylor and Francis Online.
The effective dissolution of refractory plutonium oxide (fired to T 1000°C) can be carried out by forming ceric nitrate in nitric acid. Preliminary engineering concepts are presented for dissolving such actinide species in the presence of contaminated high-efficiency particulate air (HEPA) filters and incinerator ashes to permit actinide recovery using conventional wet methods. An electrochemical oxidation tank is envisioned with electrodes mounted on the tank lid to facilitate remote operation and maintenance. Contaminated HEPA filters can be treated using an upflow reactor in which ceric nitrate is recirculated between an oxidation tank and a reactor. A membrane separating the electrodes is not required, but special materials of construction are required for all equipment in direct contact with ceric nitrate (e.g., titanium or glass-lined vessels). Since this oxidant is easily reduced to cerous nitrate using oxalic acid, subsequent actinide recovery can be carried out in conventional stainless steel equipment after reduction. The concepts described have been demonstrated on the bench scale.