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The first operation is done in the pin chopper. Intact fuel pins are prepared for<br />

electrorefining by chopping them into short segments, exposing the fuel, and<br />

removing scrap such as the spacer wire, end caps, and plenum. The highly<br />

radioactive fuel is then introduced into the electrorefiner in perforated steel baskets.<br />

Shown in Figure 8-5, the electrorefiner consists of the process vessel with<br />

associated heater/insulator assembly, cover, and support stand; electrode assemblies<br />

(anodes and cathodes) and their associated handling and placement mechanisms;<br />

ancillary systems for cover gas circulation, stirring, materials addition, sampling,<br />

and measurements; and an instrumentation and control system. A staging or support<br />

station services the electrorefiner. It attaches and removes anode and cathode parts,<br />

removes product from the cathodes, and empties the cladding hulls from the anode<br />

baskets. The design is based on the engineering-scale electrorefiner in service in the<br />

Chemical Technology Division at the Illinois site since 1987 and still ongoing.<br />

Figure 8-5. Schematic of electrorefiner<br />

The electrorefiner operates at a temperature of 500 o C. It has a layer of molten<br />

cadmium, ten centimeters thick under thirty-six centimeters of molten salt. It is<br />

heated by the thermal radiation from a furnace assembly of resistance heaters in<br />

low-density ceramic insulator blocks. Circular ports in the steel cover and thermal<br />

radiation baffles provide access for four electrodes, 28 cm in diameter, and a stirrer<br />

20 cm in diameter. Other smaller ports allow material additions, sampling<br />

measurement, and cover gas control. The electrode assemblies have a long shaft<br />

with an adapter for an anode or a cathode bottom fixture, a rotation motor, rotating<br />

electrical contacts, a port cover, a containment housing, and various instrumentation<br />

175

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