This work reports the results of experiments carried out in a sequencing ba
tch reactor (SBR) operated under 24 hour cycles, treating an effluent conta
ining a mixture of oil field wastewater and sewage, in different percentage
s. The removal of phenols, ammonium. and COD was monitored in several exper
imental runs, varying the dilution degree of the oilfield wastewater (10 to
45% v/v). The volatile suspended solids (VSS) content in the reactor was a
lso monitored and the protein (PTN) and polysaccharide (PS) contents of the
suspended biomass were determined. The removal of ammonium and phenols did
not vary significantly in the experimental runs, attaining average values
of 93% and 65%, respectively. COD removal efficiencies in the range of 30 t
o 50% were attained in the experiments carried out with dilution percentage
s of 45 and 35% (v/v) respectively. An experiment carried out with a lower
proportion of produced water (15% v/v), keeping the salinity level correspo
nding to a higher proportion of industrial effluent (45% v/v), led to an im
provement in the COD removal, indicating that the recalcitrance of the orga
nic compounds found in the effluent is the main cause of the moderate COD r
emoval efficiencies attained in the SBR system. With regard to the composit
ion of the microbial flocs, no significant variation was observed in the PS
/PTN, PS/VSS and PTN/VSS ratios when the effluent composition changed (incr
eased salinity and levels of organic material).