This article examines the use of alkali [NaOH or Ca(OH)2] and alum [Al
2(SO4)3] to reduce AOX (adsorbable organic halogen) and COD (chemical
oxygen demand) in chlorine-stage (C-stage) effluent for hardwood kraft
pulps. Tests were conducted on the whole effluent and on its molecula
r-weight fractions. The results indicate that 80% of the AOX in the C-
stage effluent can he removed by treating the effluent with NaOH at pH
12.5 prior to conventional sedimentation with alum. Ether extraction
of the hardwood C-stage effluent before and after chemical treatment s
uggests that these extractives are the primary source of residual AOX.