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Experimental and modeling approach to study sorption of dissolved hydrophobic organic contaminants to microbial biofilms

机译:实验和建模方法研究溶解的疏水性有机污染物对微生物生物膜的吸附

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摘要

A biofilm reactor was developed to investigate the sorption of polycyclic aromatic hydrocarbons (PAH) as model compounds for hydrophobic organic contaminants (HOC) to intact microbial biofilms at environmentally realistic concentrations. When operated as a differential column batch reactor, the system can be used to study the thermodynamics as well as the kinetics of the exchange of HOC between an aqueous phase and microbial biofilms. Organic carbon normalized partition coefficients (Koc) for phenanthrene, fluoranthene and pyrene were at the lower end of those known for other organic sorbents. Intra-biofilm diffusion coefficients (D) were calculated from decrease in solute concentration over time using a model for diffusion through a plane sheet and ranged from 0.23 to 0.45×10−9 cm2 s−1 for the three PAH. These diffusion coefficients are about four orders of magnitude lower than those reported in literature for free aqueous solution. These data and the experimental approach presented here are useful to assess the importance of microbial biofilms for exchange processes of HOC in heterogeneous systems such as water distribution systems, membranes and aquifers, sewer systems or surface soils.
机译:开发了一种生物膜反应器,以研究多环芳烃(PAH)作为疏水性有机污染物(HOC)的模型化合物在环境中实际浓度下对完整微生物生物膜的吸附。当作为差分塔间歇反应器运行时,该系统可用于研究水相与微生物生物膜之间HOC交换的热力学以及动力学。菲,荧蒽和pyr的有机碳归一化分配系数(Koc)在其他有机吸附剂已知的较低端。使用穿过平板的扩散模型,根据溶质浓度随时间的降低来计算生物膜内扩散系数(D),三个PAH的生物膜扩散系数在0.23至0.45×10-9 cm2 s-1之间。这些扩散系数比游离水溶液的文献报道的扩散系数低大约四个数量级。此处提供的这些数据和实验方法对于评估微生物生物膜对于异质系统(如水分配系统,膜和含水层,下水道系统或表层土壤)中HOC交换过程的重要性非常有用。

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