A rotary vacuum filter is available with an area of 200 m2 and vacuum pressure of 75 kPa. Filter leaf tests have been performed on a cell broth with a viscosity of 5 cP. The leaf tests gave a specific cake resistance of 1×1011 cm/g and medium resistance of 1×108 cm-1. The cake solids (dry basis) per volume of filtrate was 15 g/L. It is desired to operate the large filter with cycle time of 45 s and a cake formation time of 10 s. What is the filtration rate expected for the rotary vacuum filter? How significant is the resistance medium?
Expert's answer
For rotatry filter we know that V=(2KAP)^1/2 where K=k/(1-)/C0 now A= area, P=pressure and k=cake permeability,
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