) and untreated sludge (
) are now distinct. K(
)=3.53 ±
0.45 m/h ; r=0.97 / K(
)=2.50 ± 0.28 m/h ; r=0.98. |
| Figure 5b: This figure represents the result of the method bringing the
height of the sludge in the graduated cylinder as quickly as possible to
different volumes values (Vasc=VGD). One sees that the straight slopes for
treated AS (
) and untreated sludge (
) are now distinct. K(
)=3.53 ±
0.45 m/h ; r=0.97 / K(
)=2.50 ± 0.28 m/h ; r=0.98. |
