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44<br />

Realative pore volume (%)<br />

100<br />

10<br />

1<br />

1,E +00 1,E +01 1,E +02 1,E +03 1,E +04 1,E +05 1,E +06<br />

Pore radius (nm)<br />

Figure 1: Pore size distribution curve in double logarithmic representation for calcium silicate<br />

For the calcium silicate board with bulk density of 250 kg/m3 the relative pressure‐volume data<br />

were determined by the 2002 mercury intrusion porosimeter and the micropore unit 120 of<br />

ERBA Science, enabling the determination of pores with radii from 3.7 nm up to 0.06 mm. The<br />

pore size distribution was determined from the volume intruded at each pressure increment.<br />

Total porosity was determined from the total volume intruded. The specific surface area of<br />

pores was calculated from the pore radii and the pore volumes. The obtained cumulative pore<br />

size distribution curve for calcium silicate is in figure 1.<br />

The pore volume ‐ pore size distribution curve in a double logarithmic representation can be<br />

divided into the pore space fractions characterized by a constant slope and indicating the ranges<br />

of self‐similarity. The slope of each fraction gives the fractal dimension FD of the pores in the<br />

fraction.<br />

The mean fractal dimension of a relevant pore volume consisting of i fractions is calculated<br />

according to the relationship:<br />

∑ FDi<br />

⋅log(<br />

rmax<br />

i / rmin<br />

i )<br />

i FDm<br />

=<br />

log(<br />

rmax<br />

/ rmin<br />

)<br />

(2)<br />

where rmaxi, rmini are the maximum and minimum pore radii of particular fractions, rmax,<br />

rmin are maximum and minimum pore radii of the relevant volume.<br />

3 Transport parameters model<br />

Generally the effective transport parameter can be expressed by a power function model in<br />

which the transport parameter Ki of the ith continuous material component (solid, gaseous,<br />

liquid) contributing mostly to the transport can be approximated according to the relation [4]:

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