Treatment of landfill leachate in a bench scale MBR

被引:16
作者
Svojitka, J. [1 ,2 ]
Wintgens, T. [1 ]
Melin, T. [2 ]
机构
[1] Univ Appl Sci NW Switzerland, Sch Life Sci, Inst Ecopreneurship, CH-4132 Muttenz, Switzerland
[2] Rhein Westfal TH Aachen, Chair Chem Proc Engn, D-52056 Aachen, Germany
关键词
Landfill leachate; Membrane bioreactor; Bisphenol A; BISPHENOL-A; DENITRIFICATION; DEGRADATION; INHIBITION; GROWTH;
D O I
10.5004/dwt.2009.763
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
In the present work, a bench-scale MBR plant treating landfill leachate was operated for a period of 6 months. The volume of the activated sludge tank was approx. 50 L and it was coupled with a polyethersulphone (PES) tubular membrane with pore size in the ultrafiltration range. The monitoring of the pilot plant was aimed at biological parameters (removal of nitrogen, COD and BOD) and filtration properties of the membrane (permeabilities in relation to cross-flow velocity, trans-membrane pressure and sludge concentration). Because of the high content of xenoestrogenic substances in the landfill leachates, the concentration of bisphenol A (BPA) was followed in influent, mixed liquor and permeate. Regarding the results on carbon removal, overall COD removal was less than 30% in most cases, while BOD removal was 91%. Nitrification efficiency was 90-99% (decrease of ammonia nitrogen from 1200 mg/L to 10-150 mg/L), denitrification was only possible after addition of external substrate (methanol). Removal of BPA was highly efficient - from an initial concentration in the influent of 2100 mu g/L to less than 1 mu g/L in the effluent. The membrane permeabilities varied from 3.5 to 40 L/(m(2)/h/bar) (LMH/bar) depending on the operational conditions (cross-flow velocity, trans-membrane pressure and biomass concentration).
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页码:136 / 141
页数:6
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