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Interpretation of hydrocarbon plume biodegradation in 2-D bench-scale tank experiments by reactive transport modelling

机译:反应运输建模对二维长凳罐实验中的碳氢化合物羽流生物降解

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High resolution reactive transport modelling was applied as a tool for a model-based interpretation of detailed laboratory experiments on the interplay of transverse mixing and aerobic and anaerobic hydrocarbon biodegradation. As a typical groundwater contaminant, ethylbenzene (as a mixture of unlabelled and fully deuterium-labelled isotopologues) was continuously injected into a 2-D bench-scale flow-through tank through a central inlet port, generating a hydrocarbon plume along the whole length of the tank. During the first phase of the experiment, where the tank was recharged with water containing oxygen as the major dissolved electron acceptor, the aerobic strain Pseudomonas putida Fl was inoculated in order to initiate aerobic biodegradation of the ethylbenzene. Later, nitrate was added as an additional electron acceptor and the denitrifying strain Aromatoleum aromaticum EbN1 was inoculated to study competitive degradation under aerobic / anaerobic conditions. The spatial distribution of anaerobic degradation was investigated using measurements of compound-specific stable isotope fractionation along a vertical profile at the tank outlet. The numerical model was calibrated to fit the measured concentration profiles of these compounds at the outlet ports. Simulated and measured ethylbenzene and oxygen concentrations showed a good agreement for the aerobic degradation phase of the experiment, while the evaluation of the aerobic/anaerobic phase with competitive biodegradation was ambiguous due to uncertainties regarding the actual stoichiometry of the specific denitrification reaction. The model results, calibrated on the stable isotope signatures, showed that for the case of aerobic/anaerobic degradation the observed isotopic pattern strongly depends on the assumed initial distribution of microbial biomass.
机译:高分辨率反应运输建模应用于用于横向混合和有氧和厌氧烃生物降解的相互作用的基于模型的诠释的工具。作为典型的地下水污染物,通过中央入口将乙苯(作为未标记的和完全氘标记同位素的混合物)连续地注入2-D台级流通罐中,沿着整个长度产生碳氢化合物羽流坦克。在实验的第一阶段,其中用含有氧气作为主要溶解电子受体的水再充电,可以接种有氧菌株Pseudomonas pivida fl以开始乙苯的有氧生物降解。后来,加入硝酸盐作为额外的电子受体,并接种反硝化菌株芳族芳香族芳香族EBN1,以研究有氧/厌氧条件下的竞争降解。使用沿罐出口处的垂直轮廓的垂直轮廓的垂直轮廓测量来研究厌氧降解的空间分布。数值模型被校准以适合在出口处的这些化合物的测量浓度曲线。模拟和测定的乙苯和氧浓度表现出对实验的好氧降解阶段的良好一致性,而具有竞争性生物降解的有氧/厌氧相的评价是模糊的,由于关于特定反硝化反应的实际化学计量的不确定性。在稳定的同位素签名上校准的模型结果显示,对于有氧/厌氧降解的情况,观察到的同位素模式强烈取决于微生物生物量的假定初始分布。

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