Özet
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.
| Orijinal dil | İngilizce |
|---|---|
| Sayfa (başlangıç-bitiş) | 239-251 |
| Sayfa sayısı | 13 |
| Dergi | Water, Air, and Soil Pollution |
| Hacim | 126 |
| Basın numarası | 3-4 |
| DOI'lar | |
| Yayın durumu | Yayınlandı - 2001 |
BM SKH
Bu sonuç, aşağıdaki Sürdürülebilir Kalkınma Hedefine/Hedeflerine katkıda bulunur
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SKH 6 Temiz Su ve Sanitasyon
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SKH 7 Erişilebilir ve Temiz Enerji
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