A pilot-scale upflow anaerobic sludge blanket (UASB) reactor was emplo
yed to treat the wastewater of a purified-terephthalic-acid (PTA) manu
facturing factory. The performance of UASB reactor in terms of COD rem
oval was achieved 62% at the volumetric loading rate of 2.93 kg COD/m(
3)/day. One of the major constituents, p-toluic acid in PTA wastewater
was the refractory component due to the methyl substituent on the aro
matic ring, which restricted the biodegradation performance. Moreover,
from our study, it was surprising that high concentration of acetic a
cid would retard the degradation of aromatics in the sludge bed. A con
trol strategy of acetic acid level in the sludge bed was suggested dur
ing the start-up period. Comparison of the anaerobic biodegradability
of aromatic substituents in PTA wastewater was concluded as the follow
ing sequence: -COOH > -CHO greater than or equal to -CH3 in terms of t
he derivative functional groups based on the benzoic acid. Observation
of bacterial population of the sludge granules showed high diversity
of syntrophic structure on the biogranular surface as well as acetocla
stic methanogens. (C) 1997 IAWQ. Published by Elsevier Science Ltd.