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THORIUM AS AN ENERGY SOURCE - Opportunities for Norway ...

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The Back End of the Thorium Fuel Cycle<br />

substance is dissolved in nitric acid and separated by solvent extraction. Thorium is considerably<br />

less amenable than uranium to such processing.<br />

Reprocessing difficulties are especially severe with HTR-type fuels of whatever composition, since<br />

the particle coatings and graphite matrix are chemically resistant and troublesome to break down<br />

mechanically.<br />

6.3.1 The “Head-End” Operations<br />

The aim of these operations is to obtain, after preliminary operations leading to dissolution, a<br />

solution of U-Th nitrates together with a small quantity of minor actinides and fission products.<br />

Extraction of U-233 from irradiated thorium rods was conducted extensively in the US from the<br />

1950s until the 1970s. Almost 700 tonnes thorium were irradiated, delivering more than 1.5<br />

tonnes of U-233. The separation operations were piloted at ORNL in the THOREX plant, and in<br />

the Knolls Atomic Power Laboratory. The process was later adapted to the Great “canyon” plants<br />

at Han<strong>for</strong>d and Savannah River (SRP), and the commercial direct maintenance plant of Nuclear<br />

Fuel Services at West Valley near Buffalo, now being dismantled, which reprocessed the first core<br />

of Indian Point 1 (95% ThO2, 5% U-235O2), but without recovering thorium (which was left in the<br />

waste).<br />

The processes are explained in an interesting paper [146], which is one of the early documents<br />

giving details of the processes and of the adaptation of these large PUREX-type plants to the<br />

THOREX processes (Figure 6.3).<br />

Figure 6.3: Outline of the THOREX Process (Thorium Extraction).<br />

Head-end operations <strong>for</strong> fertile fuels to extract U-233: Due to its great stability, dissolution of<br />

thorium or ThO2 is not as straight<strong>for</strong>ward as that of U, and especially of UO2. Strong nitric acid<br />

with HF is required, and the process takes a rather long time, especially <strong>for</strong> high temperature<br />

sintered compact ThO2. Dissolution can take up to 35 hours. To prevent corrosion of the<br />

equipment by HF, aluminium nitrate was added as a buffer.<br />

Similar processes have been used in India on a small scale <strong>for</strong> thorium and ThO2 rods and in<br />

other countries (UK at Dounray, Canada at Whiteshell, Germany at Jülich and Karlsruhe). In<br />

75

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