Experimental measurements were made of the average specific cake resistance
during the initial period of cake filtration, and the theoretical calculat
ions about the period were also performed. The "filtration-permeation metho
d" in the filtration cell of small area was used to measure the flow rate d
uring the initial period of filtration, which is essentially characterized
by the large flux due to fast now rate and the rapid change of flow rate wi
thin a relatively short time interval. The measured average specific cake r
esistances of thin cakes which represent the cakes of initial period had ve
ry large values compared to the overall average specific cake resistance. T
his experimental result was contrary to the conventional theory about the i
nitial period. Applying the 'unified theory on solid-liquid separation" to
the initial period, the average specific cake resistances at the initial pe
riod can have the large values-more than two times greater than that of the
overall value.