Knowledge of toxic chemical sorption by soil/sediment is critical for environmental risk assessment of toxic chemicals, especially for the multi-sorbate system in river ecosystem. Sorption characteristics of 2, 4-Dichlorophenol, 2, 4-Dinitrophenol and 2, 4-Dimethyphenol on sediment were investigated. Adsorption isotherms in single- and multi-sorbate systems fitted well the Freundlich model. The adsorption effects were different among three selected phenolic compounds in single- and multi-sorbate systems. The synergetic affect that 2, 4-Dinitrophenol and 2, 4-Dimethyphenol bring to 2, 4-Dichlorophenol can be explained by the compression of double electronic layer and the charge neutrality. Adsorption kinetic results showed that pseudo-second-order model can be used to describe the experimental data and the adsorption affinity of phenolic compounds influenced greatly by the adsorption velocity. The present study suggests that the fate and transport of emerging pollutants such as phenolic compounds could be affected in the presence of different hydrophobic pollutants in aquatic systems. 相似文献
The occurrence and removal of eight endocrine disrupting compounds (EDCs), including estrone (E(1)), 17β-estradiol (E(2)), estriol (E(3)), 17α-ethinylestradiol (EE(2)), diethylstilbestrol (DES), bisphenol A (BPA), nonylphenol (NP) and octylphenol (OP), and their estrogenicities were investigated in a sewage treatment plant in Harbin city, China. The EDCs were extracted from wastewater samples by solid phase extraction (SPE) method and analyzed with gas chromatography coupled with mass spectrometry (GC-MS). The average concentrations in the influents and effluents ranged from 6.3 (EE(2)) to 1725.8 ng L(-1) (NP) and from 相似文献
Performance and microbial community composition were evaluated in a two-phase anaerobic and aerobic system treating sulfate-rich cellulosic ethanol wastewater (CEW). The system was operated at five different chemical oxygen demand (COD)/SO42− ratios (63.8, 26.3, 17.8, 13.7, and 10.7). Stable performance was obtained for total COD removal efficiency (94.5%), sulfate removal (89.3%), and methane production rate (11.5 L/day) at an organic loading rate of 32.4 kg COD/(m3·day). The acidogenic reactor made a positive contribution to net VFAs production (2318.1 mg/L) and sulfate removal (60.9%). Acidogenic bacteria (Megasphaera, Parabacteroides, unclassified Ruminococcaceae spp., and Prevotella) and sulfate-reducing bacteria (Butyrivibrio, Megasphaera) were rich in the acidogenic reactor. In the methanogenic reactor, high diversity of microorganisms corresponded with a COD removal contribution of 83.2%. Moreover, methanogens (Methanosaeta) were predominant, suggesting that these organisms played an important role in the acetotrophic methanogenesis pathway. The dominant aerobic bacteria (Truepera) appeared to have been responsible for the COD removal of the SBR. These results indicate that dividing the sulfate reduction process could effectively minimize sulfide toxicity, which is important for the successful operation of system treating sulfate-rich CEW.