The moving bed biofilm process is based on plastic carriers on which biomas
s attaches and grows. The original Kaldnes carrier was made of high-density
polyethylene (density 0.95 gcm(-1)) that could be used in filling fraction
s (volume of carriers in empty reactor) up to 70% that gives a specific are
a of 350 m(2)m(-3), Lately there has been an interest in the use of larger
carrier elements, especially when using the process for upgrading of activa
ted sludge plants. This paper analyses the influence of the carrier size an
d shape on performance, especially related to highly loaded plants working
on municipal wastewater. The results demonstrate that moving bed biofilm re
actors should be designed based on surface area loading rate (g COD/m(2)d)
and that shape and size of the carrier do not seem to be significant as lon
g as the effective surface area is the same. The results indicate that very
high organic loads can be used in order to remove soluble COD but that the
settleability of the sludge is negatively influenced at high loading rates
.