The hybrid process resulting from adding powdered activated carbon (PAC) to
ultrafiltration (UF) reactors is being used to remove organic compounds in
full-scale drinking water treatment plants. One way to increase the adsorp
tion efficiency of PAC is to add it to continuously stirred tank reactors (
CSTRs) or to plug flow reactors installed upstream of the membranes. additi
onally, the PAC that is recovered from the membrane backwash can be recycle
d to a flee blanket reactor (FBR) installed upstream of the PAC/CSTR-UF pro
cess. This study developed an adsorption model that predicts the removal of
dissolved organic carbon (DOC) in the FBR-PAC/CSTR-UF system. The model wa
s verified experimentally using two commercially available PACs in a labora
tory-scale pilot unit. Removal of DOC by coagulation with aluminum salts an
d adsorption on the recycled PAC in the FBR substantially reduced carbon us
e. The model was used to assess the effect of various operating parameters
on DOC adsorption efficiency and to determine optimal operating conditions.