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Euradwaste '08 - EU Bookshop - Europa

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Figure 3.3.1 Emplacement of SF-Canister - Start niche and lock to the emplacement tunnel<br />

(schematic)<br />

Bentonite granulate<br />

Emplacement trolley Bentonite granulate<br />

SF Canister and pedestal of bentonite blocks<br />

248<br />

Backfilling device with twin auger<br />

Figure 3.3.2: Emplacement trolley with spent fuel canister at emplacement position (left); Wagon<br />

emplacing bentonite granulate in disposal tunnel after a waste canister has been emplaced (right)<br />

Results within ESDRED<br />

The objectives of Nagra’s bentonite emplacement testing within the EC-supported project ESDRED<br />

were as follows:<br />

• Testing and demonstrating of suitable granular buffer installation techniques on a full scale<br />

in surface facilities;<br />

• Verification if the requirements can be fulfilled.<br />

The general objectives and the experiences from previous experiments lead to an ambitious project<br />

specific target value for the emplacement dry density of about 1500 kg/m 3 . In previous experiments<br />

Nagra executed various tests with different bentonite types for buffer material. Because of its favorable<br />

properties with respect to technical emplacement, bentonite granulate is used in Nagra’s reference<br />

concept. Although small-scale laboratory experiments were performed several years ago, a<br />

large scale test was felt to be advantageous to improve confidence that the required dry density of<br />

emplaced bentonite granulate can actually be reached.<br />

For this project Wyoming bentonite from Amcol Speciality Minerals was used. The sodiumbentonite<br />

MX-80 was delivered in a conditioned, slightly granulated state to improve the pourability<br />

and the granulation. The production of the granulated material was done in the Rettenmaier facilities<br />

in Holzmühle, Germany. During the granulation of the bentonite, an increase of the bulk<br />

grain dry density from 1.17 g/cm 3 to 2.10 g/cm 3 with simultaneous halving of porosity was<br />

achieved.<br />

The built twin auger system (Figure 3.3.3) to emplace the granulated buffer material has a total<br />

length of about 9 m and a weight of 1350 kg. The length of the two auger casings is 7.0 m, the diameter<br />

of the tubes are 0.2 m. The feed rate can be controlled by the auger turning speed. The rotat-

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