The pulp- and paper-industry generates large volumes of highly heterog
enous wastewaters containing compounds from wood or other raw material
, process chemicals and compounds formed during processing. The wastew
aters from mechanical pulping and secondary fiber pulping as well as t
he condensates from chemical and semi-chemical pulping are typically n
on-toxic to methanogenic degradation and contain easily degradable org
anic compounds. Consequently, anaerobic digestion is an attractive tre
atment alternative for these effluents. In addition, both primary and
secondary sludges from pulp- and paper-industry wastewater treatment-p
lants are amenable to anaerobic digestion. In contrast, the bleaching
effluents from chemical pulping, the debarking effluents as well as th
e CTMP effluents are likely to be inhibitory to methanogenic degradati
on; also their biodegrability is relatively low. Dilution with other w
astewater streams or detoxification by various pretreatments have been
used to facilitate anaerobic treatment of these inhibitory wastewater
s. The potential of the anaerobic systems for reductive dechlorination
and sulfur recovery is unique and of great interest. In almost all pu
lp- and paper-industry full-scale applications, anaerobic treatment is
followed by aerobic post-treatment. The suitability and the cost of t
he anaerobic-aerobic and aerobic treatment-systems are largely affecte
d by a variety of mill-specific factors.