Enhanced concentrations of phosphorus entering the aquatic systems hav
e been linked with eutrophication and its associated problems. The EC
Urban Wastewater Treatment Directive, adopted in May 1991, included ef
fluent standards for phosphorus in the U.K. for the first time. The ne
ed for an efficient and cost-effective phosphorus removal process has
now become apparent. Two pilot-scale columns, an aerated filter packed
with seeded expanded shale and an anoxic filter packed with plastic m
edia, were operated using settled sewage feed. Iron (II) sulphate hept
ahydrate solution was dosed onto the top of the aerated filter at vary
ing ratios of total phosphorus to iron. The performance of the plant w
ith respect to BOD, GOD, TKN and suspended solids removal was unaffect
ed by chemical dosing. A significant reduction of nitrification occurr
ed; however, this may be linked to increased BOD and ammonia loading.
The run time of the biological aerated filter was not significantly af
fected by chemical addition. The choice of chemical dose used depends
on the stability of process required, which increases with increasing
dose, capital available and the EC limits imposed on the effluent to b
e discharged. To meet EC requirements, the most favourable chemical do
sing ratio was 1:1.25 (weight ratio P:Fe). (C) 1997 Elsevier Science L
td.