Lab-scale sequencing batch reactors were used to treat chemithermomechanica
l pulping wastewater that had chemical oxygen demand (COD) and biochemical
oxygen demand (BOD) in the range of 5,980-8,990mg/L, and 2,240-3,190 mg/L,
respectively. A cycle time of 24 hour, with a hydraulic retention time of 3
4.3 hours was used. With I hour of settling, COD and BOD reductions of 30-4
1% and 67-78% were observed. However, with a 4-hour settling, COD and BOD r
eductions of 53-62% and 88-94% were achieved, respectively. Most of the oxy
gen demand reductions occurred within the first 16 hours of aeration. Adjus
tment of pH did not result in significant improvement in COD removal. Resin
acids and fatty acids concentrations in the CTMP wastewater were reduced i
n the SBR process; however, they were still not fully detoxified in the eff
luent.