TY - JOUR
T1 - Assessment of biogas use as an energy source from anaerobic digestion of brewery wastewater
AU - Kasapgil Ince, Bahar
AU - Ince, Orhan
AU - Anderson, G. Ken
AU - Arayici, Semiha
PY - 2001
Y1 - 2001
N2 - Energy recovery from a crossflow ultrafiltration (UF) membrane unit employed in order to improve the performance of an anaerobic contact digester for the treatment of brewery wastewater was assessed. The performance of the pilot-scale anaerobic UF membrane system was studied for over 15 months. At steady-state conditions, an organic loading rate of 28.5 kg COD m-3 d -1, a hydraulic retention time of 4.2 days and overall COD and BOD removal efficiencies of 99% and almost 100% were achieved, respectively. Percent methane in biogas was found to be in a range of 67-79% with the corresponding methane yield of 0.28-0.35 m3 CH4 kg -1 COD removed. The potential energy recovery from the system treating brewery wastewater at an OLR of 28.5 kg COD m-3 d-1 was 87 MJ d -1 which would enable to maintain all energy requirements of the feed pump, mixing and heating of the reactor contents. In addition to this, 71% of the energy requirement for recirculating the reactor content through the membranes would also be recovered.
AB - Energy recovery from a crossflow ultrafiltration (UF) membrane unit employed in order to improve the performance of an anaerobic contact digester for the treatment of brewery wastewater was assessed. The performance of the pilot-scale anaerobic UF membrane system was studied for over 15 months. At steady-state conditions, an organic loading rate of 28.5 kg COD m-3 d -1, a hydraulic retention time of 4.2 days and overall COD and BOD removal efficiencies of 99% and almost 100% were achieved, respectively. Percent methane in biogas was found to be in a range of 67-79% with the corresponding methane yield of 0.28-0.35 m3 CH4 kg -1 COD removed. The potential energy recovery from the system treating brewery wastewater at an OLR of 28.5 kg COD m-3 d-1 was 87 MJ d -1 which would enable to maintain all energy requirements of the feed pump, mixing and heating of the reactor contents. In addition to this, 71% of the energy requirement for recirculating the reactor content through the membranes would also be recovered.
KW - Anaerobic contact digester
KW - Brewery wastewater
KW - Crossflow ultrafiltration
KW - Energy recovery
UR - http://www.scopus.com/inward/record.url?scp=0035136407&partnerID=8YFLogxK
U2 - 10.1023/A:1005236731131
DO - 10.1023/A:1005236731131
M3 - Article
AN - SCOPUS:0035136407
SN - 0049-6979
VL - 126
SP - 239
EP - 251
JO - Water, Air, and Soil Pollution
JF - Water, Air, and Soil Pollution
IS - 3-4
ER -