Sewage sludge is known to be a poorly dewaterable material. In order to improve the dewatering performance, new techniques have been explored in recent years. A frequently studied technique is electro-dewatering, in which the pressure-driven dewatering operation is assisted by an electric field, thus yielding faster dewatering kinetics and improved final cake dry matter contents by means of electro-osmotic water transport. As special setup has been build to measure this process in the NMR. This setup is given in figure 1.
Using this setup the dewatering was
measured for various electric currents. These currents were
applied after 45min (2700 s) of pressure dewatering, and the
applied pressure was maintained until the end of the dewatering
run. The result are given in figure 2.
Fig.
2 : Spatio-temporal sludge solidosity profiles during
(electro)dewatering, as determined by the NMR , for 4
electric currents (0, 15, 30 and
45 mA). The currents were applied after 2700 s of pressure
dewatering, as indicated by the thick
black lines in the center parts
of the subplots. The colorbar represents the solidosity color
code used in all subfigures.
In the mere pressure dewatering run (Fig. 2a), the expression
slows down quickly, resulting in a profile with moderate
solidosity at the filter medium and lower but rather uniform
solidosity above the filter medium. In the cases where an electric
current is applied from 45min onwards (Figs.2b–d,), it is seen
that near the end of the pressure dewatering stage the profiles
seem to slow down significantly, because of the limitations of the
pressure dewatering operation. Once the electric current is
applied, at 2700 s, the profiles show a quick decrease again in
cake thickness and an overall increase in solidosity. The speed of
the decrease in cake thickness and increase in solidosity is
clearly linked to the applied current as can be seen from a
comparison of the profile evolution for 15, 30 and 45mA.