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生物膜反应器(慢滤池)能否去除活性污泥处理中难以去除的有机微量污染物?

Can those organic micro-pollutants that are recalcitrant in activated sludge treatment be removed from wastewater by biofilm reactors (slow sand filters)?

机构信息

Environmental Science, Aarhus University, Frederiksborgvej 399, 4000 Roskilde, Denmark.

Environmental Science, Aarhus University, Frederiksborgvej 399, 4000 Roskilde, Denmark.

出版信息

Sci Total Environ. 2015 Feb 15;506-507:315-22. doi: 10.1016/j.scitotenv.2014.10.113. Epub 2014 Nov 22.

DOI:10.1016/j.scitotenv.2014.10.113
PMID:25460965
Abstract

The degradation of seven compounds which are usually recalcitrant in classical activated sludge treatment (e.g., diclofenac, propranolol, iopromide, iohexol, iomeprol tebuconazole and propiconazole) was studied in a biofilm reactor (slow sand filtration). This reactor was used to treat real effluent-wastewater at different flow rates (hydraulic loadings) under aerobic conditions so removal and degradation kinetics of these recalcitrant compounds were calculated. With the hydraulic loading rate of 0.012 m(3)m(2)h(-1) the reactor removed 41, 94, 58, 57 and 85% of diclofenac, propranolol, iopromide, iohexol and iomeprol respectively. For these compounds the removal efficiency was dependent on hydraulic residence-times. Only 59 and 21% of the incoming tebuconazole and propiconazole respectively were removed but their removal did not depend on hydraulic residence time. Biofilm reactors are thus efficient in removing micro-pollutants and could be considered as an option for advanced treatment in small wastewater treatment plants.

摘要

在生物膜反应器(慢砂滤池)中研究了通常在经典活性污泥处理中难降解的七种化合物(如双氯芬酸、普萘洛尔、碘普罗胺、碘海醇、碘美普尔、噻康唑和丙酸氟替卡松)的降解情况。该反应器用于在需氧条件下以不同流速(水力负荷)处理实际废水,因此计算了这些难降解化合物的去除和降解动力学。在水力负荷为 0.012 m(3)m(2)h(-1)时,反应器分别去除了 41%、94%、58%、57%和 85%的双氯芬酸、普萘洛尔、碘普罗胺、碘海醇和碘美普尔。对于这些化合物,去除效率取决于水力停留时间。仅去除了 59%和 21%的噻康唑和丙酸氟替卡松,但它们的去除并不取决于水力停留时间。因此,生物膜反应器在去除微量污染物方面非常有效,可以被视为小型污水处理厂的高级处理选项。

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