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Fuel loading process begins at Palisades
The Palisades nuclear power plant has drawn closer to restart, as plant staff began the process of loading fuel into the reactor vessel on Sunday morning.
The commencement of fuel loading places the Covert, Mich., facility in Mode 6—or the refueling stage—under the plant’s technical specifications, plant owner and operator Holtec International said in a news release. The Palisades reactor core consists of 204 fuel assemblies that include new fuel and partially used fuel from the plant’s most recent operating cycles. According to Holtec, the fuel loading is being conducted in accordance with plant procedures and technical specifications.
Satyabrata Mishra, Vishnu Anand P, Gnanasoundari J, Rajeev R, Desigan N, Venkatesan K A
Nuclear Science and Engineering | Volume 199 | Number 6 | June 2025 | Pages 988-999
Research Article | doi.org/10.1080/00295639.2024.2398358
Articles are hosted by Taylor and Francis Online.
Tri-iso-amyl phosphate (TiAP) is being proposed as a suitable alternate to tri-butyl phosphate mainly for the reprocessing of high-Pu-content spent fuel from fast reactors. After its use in a few cycles, the solvent has to be categorized as organic waste, which needs further treatment and disposal. Toward this, systematic studies have been carried out on the alkaline hydrolysis of TiAP in n-dodecane (n-DD) using sodium hydroxide (NaOH). The experiments were carried out in a stainless steel autoclave with a reactor vessel having a 1 L processing capacity. The parameters, such as mixing intensity, temperature, aqueous-to-organic phase volume ratio, and initial NaOH concentration, that can affect the kinetics of the hydrolysis reaction were studied. During each experiment, the TiAP concentration in the organic phase decreased steadily with time followed by a sudden decrease, which could be due to the autocatalytic hydrolysis of TiAP. After the completion of the hydrolysis reaction, the organic phase was mainly n-DD with iso-amyl alcohol, suggesting complete hydrolysis of TiAP to its aqueous-soluble hydrolysis products. Based on the studies, it was observed that temperature and initial NaOH concentration, among other parameters, highly influence the rate of hydrolysis of TiAP.