|Title||Improving the energy efficiency of a pilot-scale UASB-digester for low temperature domestic wastewater treatment|
|Author(s)||Xu, Shengnan; Zhang, Lei; Huang, Shengle; Zeeman, Grietje; Rijnaarts, Huub; Liu, Yang|
|Source||Biochemical Engineering Journal 135 (2018). - ISSN 1369-703X - p. 71 - 78.|
Sub-department of Environmental Technology
Meteorology and Air Quality
|Publication type||Refereed Article in a scientific journal|
|Keyword(s)||Anaerobic domestic wastewater treatment - Energy saving - Low temperature - Methanogenic activity - UASB-digester|
A pilot-scale UASB-Settler-Digester (USD) system was utilized to treat raw municipal wastewater collected from a sewer system at 10 °C. During the reactor operation, UASB sludge was continuously transferred from the UASB to a settler; concentrated sludge in the settler was then transferred to a digester operated at 35 °C. The results showed that the settler with a hydraulic retention time (HRT) of 3 h increased UASB sludge chemical oxygen demand (COD) concentration from 14.5 ± 2.5 g/L to 29.9 ± 4.1 g/L. With an HRT of 6 h, the USD system achieved a mean COD removal of 49.2%; and 23.9% influent COD was converted to methane. The specific methanogenic activities at 35 °C of the UASB and the digester sludge were 0.26 and 0.24 g CH4 COD/(g VSS d), respectively, and the stability values were 0.21 and 0.16 g CH4 COD/g COD, respectively. The stability of the settled sludge was similar to that of the recirculated UASB sludge. Compared to a UASB-digester system, the system with an added settler achieved similar COD removal and methane production, but reduced sludge recirculation rate (from 16% to 8% of the influent flow rate), which led to a 50% heating energy saving in the digester of the UASB-digester.