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Modified Bentonite Slurries for Slurry Shields in Highly ... - ETH - IGT

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Additionally, the <strong>in</strong>direct tests of 3.2 have been<br />

executed ma<strong>in</strong>ly <strong>for</strong> the sake of completeness.<br />

Sometimes the Marsh Funnel could not be employed<br />

as due to its high viscosity the suspension did not<br />

run out.<br />

It was seen (Penner and Hermanns, 1998), that add<strong>in</strong>g<br />

polymers and NaCl, to a lesser extent also HT,<br />

improved the maximum support pressure of the suspension.<br />

This is attributed to the effect, by which<br />

these additives <strong>for</strong>m network-like, favorable strutures<br />

(Fig. 5). Comb<strong>in</strong>ed addition of polymers and<br />

NaCl further improved the support<strong>in</strong>g ability. CaCl 2<br />

and CPC have a much stronger flocculation tendency<br />

than NaCl, which favors the <strong>for</strong>mation of a<br />

filter cake, but prevents penetration. Higher concentrations<br />

of CaCl 2 cancel the positive effect of polymer.<br />

Fig. 4<br />

Apparatus <strong>for</strong> measur<strong>in</strong>g the Suspension Pressure<br />

Perspex Tube (15 cm diameter)<br />

Suspension<br />

Gravel (4/8 mm)<br />

Water<br />

Air Pressure Supply<br />

In the sense of a standardized procedure, the suspensions<br />

were always mixed <strong>in</strong> the follow<strong>in</strong>g way:<br />

1. polymer was dissolved <strong>in</strong> water,<br />

2. sand was mixed with the dry bentonite, and<br />

3. other additives were stirred <strong>in</strong>to the previously<br />

mixed suspension.<br />

When mix<strong>in</strong>g the polymer it was noted that it was<br />

not completely dissolved. However, if be<strong>for</strong>e add<strong>in</strong>g<br />

the polymer the water was heated to 40 0 C (Fig. 6),<br />

the solubility was much better. This procedure was<br />

also adopted at the construction site.<br />

Our first tests aimed to better understand the<br />

mechanism of filtration. For this purpose the <strong>in</strong>fluences<br />

of Polymer (Carboxymethylcellulose), NaCl,<br />

CaCl 2 , Cetylpyrid<strong>in</strong>ium (CPC) and Hydrotalkit (HT)<br />

were exam<strong>in</strong>ed. The basic suspension was always an<br />

activated bentonite (product Ibeco HT-X), sand<br />

< 1mm and sawdust < 2mm.<br />

Fig. 6<br />

Heat<strong>in</strong>g and stirr<strong>in</strong>g the Polymer <strong>for</strong> better Solubility<br />

The next test series of experiments aimed at<br />

f<strong>in</strong>d<strong>in</strong>g from all potentially possible mixtures at least<br />

one which allowed to provide the required support<br />

pressure <strong>in</strong> Situ of 0.5 bar.. The first success was<br />

reached with a mixture consist<strong>in</strong>g (per m 3 water) of<br />

- 40 kg bentonite,<br />

- 0.5 kg polymer, and<br />

- 40 kg sawdust.<br />

However, use of this suspension <strong>in</strong> situ revealed,<br />

that the sawdust could not pass through the sieves <strong>in</strong><br />

the separation plant. Replac<strong>in</strong>g all sawdust after<br />

each cycle would have meant add<strong>in</strong>g about 16 tons<br />

per hour, which was not realistic. There<strong>for</strong>e, it was<br />

tried to determ<strong>in</strong>e the m<strong>in</strong>imum amount of sawdust<br />

required. This was found to be 10 kg, but as compensation<br />

100 kg of sand had to be added.<br />

Fig. 5<br />

Models of the aggregate structure <strong>for</strong> some additives<br />

(Penner and Hermanns, 1998)

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