Development and testing of a fully gravitational submerged anaerobic membrane bioreactor for wastewater treatment

A gravity-operated submerged anaerobic membrane bioreactor (SAnMBR) was set up in order to test its principle of operation as an alternative to conventional pumped permeation of the membrane. This operating mode allowed the membrane flux rate to be measured accurately whilst maintaining a constant t...

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Veröffentlicht in:Environmental technology. - 1993. - 36(2015), 18 vom: 05., Seite 2328-39
1. Verfasser: Pacheco-Ruiz, Santiago (VerfasserIn)
Weitere Verfasser: Heaven, Sonia, Banks, Charles J
Format: Online-Aufsatz
Sprache:English
Veröffentlicht: 2015
Zugriff auf das übergeordnete Werk:Environmental technology
Schlagworte:Journal Article Research Support, Non-U.S. Gov't AnMBR anaerobic digestion membrane fouling sustainable membrane flux wastewater treatment Biofuels Membranes, Artificial Waste Water
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520 |a A gravity-operated submerged anaerobic membrane bioreactor (SAnMBR) was set up in order to test its principle of operation as an alternative to conventional pumped permeation of the membrane. This operating mode allowed the membrane flux rate to be measured accurately whilst maintaining a constant transmembrane pressure (TMP), and allowed small transient variations in the flux rate to be observed. The reactor was operated at 36°C for a period of 115 days using a nutrient-balanced synthetic substrate with a high suspended solids concentration. Membrane cleaning was in situ by a gas scouring system using recirculation of headspace biogas. With an initial TMP of 7.0 kPa, the membrane flux slowly decreased due to membrane fouling and had not reached a constant value by day 71. The results indicated that the system was still acclimatizing up to 50 days after start-up; but from that point onwards, performance parameters became much more stable. A constant flux of 2.2 L m(-2) h(-1) was achieved over the last 45 days after the TMP was reduced to 2.3 kPa. The stable flux was maintained over this period and the loading raised to 1 g COD L(-1) d(-1) by increasing the influent strength. Under these conditions, the average chemical oxygen demand removal efficiency was 96% and the specific methane potential was 0.31 L CH4 g(-1) COD removed 
650 4 |a Journal Article 
650 4 |a Research Support, Non-U.S. Gov't 
650 4 |a AnMBR 
650 4 |a anaerobic digestion 
650 4 |a membrane fouling 
650 4 |a sustainable membrane flux 
650 4 |a wastewater treatment 
650 7 |a Biofuels  |2 NLM 
650 7 |a Membranes, Artificial  |2 NLM 
650 7 |a Waste Water  |2 NLM 
700 1 |a Heaven, Sonia  |e verfasserin  |4 aut 
700 1 |a Banks, Charles J  |e verfasserin  |4 aut 
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