铁炭微电解法降解1-丁基-3-甲基咪唑六氟磷酸盐

使用铁炭微电解法降解1-丁基-3-甲基咪唑六氟磷酸盐([BMIM]PF6),并探讨了铁炭微电解法降解[BMIM]PF6的影响因素、工艺条件及其反应动力学.结果表明,影响铁炭微电解降解[BMIM]PF6的因素按从大到小的顺序为:炭铁比、pH、反应时间;铁炭微电解降解[BMIM]PF6的最佳工艺条件是:铁粉用量3g.l-1、水样pH2.5、炭铁比2、反应时间为60—90min;在此条件下,[BMIM]PF6的去除效率可以达到90%以上且该降解反应为三级反应.     

早期胚胎发育期暴露1-辛基-3-甲基咪唑离子液体后对金鱼仔鱼的氧化损伤(Oxidative Stress of the Ionic Liquid 1-Octyl-3-Methylimidazolium Bromide on the Goldfish Larva Carassius auratus Hatching from the IL-treated Embryos)

离子液体的生物毒性受到越来越多关注,但目前该方面的研究报道很少.采用溴化1-辛基-3-甲基咪唑离子液体([C8mim]Br)处理金鱼胚胎,研究了金鱼早期胚胎发育期暴露离子液体后对金鱼仔鱼的氧化损伤.通过预实验获得金鱼胚胎(卵裂期)72小时半致死浓度(LC50)为209mg·L-1,根据该结果设计胚胎发育期离子液体的亚慢性暴露浓度为10.45mg·L-1、20.9mg·L-1、41.5mg·L-1、104.5mg·L-1.实验结果表明,与对照组相比,低浓度离子液体处理组(10.45mg·L-1和20.9mg·L-1)超氧化物歧化酶活性显著上升,高浓度处理组(41.55mg·L-1和104.55mg·L-1)极显著下降.谷胱苷肽过氧化物酶活性除10.455mg·L-1处理组为不显著上升外,其余3组均为显著下降.4个处理组丙二醛含量均比对照组显著增高,且呈现明显的剂量-效应关系.该实验结果表明,经过胚胎发育期暴露离子液体后,[C8mim]Br对金鱼仔鱼组织抗氧化系统仍产生较强的氧化损伤并引起脂质过氧化作用.因此,有必要研究离子液体对水生态系统中水生动物种群的影响,并对离子液体的生态安全做出科学评价.     

湿法脱硫烟气中多形态颗粒物的测量方法及组分特征

为全面测量固定源湿法脱硫烟气中多形态颗粒物的排放浓度及其离子组成特征，提出了一种基于一级冷凝、二级过滤和一级冲击吸收的多形态烟气颗粒物的同步测量方法，外场实测了3种湿法脱硫和除尘工艺的排放水平。现场测试表明：简易湿法除尘脱硫（NaOH法）一体化装置烟气中可过滤颗粒物（FPM）浓度为（36±11）mg/m³，可逃逸颗粒物（EPM）浓度为（33±7）mg/m³；氧化镁法+布袋除尘工艺烟气中FPM浓度为（14±5）mg/m³，EPM浓度为（13±6）mg/m³；石灰石-石膏脱硫+电袋除尘工艺烟气中FPM浓度低，小于3 mg/m³，EPM浓度为（6±1）mg/m³；烟气中EPM是传统滤膜法检测FPM浓度的0.7~5.7倍，EPM的主要存在形态为冷凝液中的可溶解颗粒物（DPM），颗粒物的组分与脱硫方法密切相关，各形态颗粒物的主要组分是SO₄^2-、SO₃^2-、NO₃^-、NO₂^-、NH₄⁺、Cl^-、Na⁺、Mg²⁺和Ca²⁺等离子。     

土壤-水稻体系中污染重金属的迁移及其对水稻的影响

在温室条件下通过水稻盆栽试验,研究了植物对添加Pb、Cd、Cu、Zn等重金属的吸收.结果表明,供试元素的迁移受本身的性质、交互作用、添加量以及土壤吸持强度所影响.植物对Pb、Cd、Cu、Zn的吸收系数与用等温吸附方程所表示的土壤吸附强度和金属元素的第一级水解常数值有关.离子冲量与稻谷产量的关系表明,它有可能作为一种污染总量控制指标,反映了总量控制中“有效态”的重要性.     

稀土矿废弃地植被恢复过程中土壤微生物演变

以福建长汀典型离子型稀土矿堆浸冶炼废弃地作为研究对象，采取"空间代时间"的方法，对堆浸废弃地不同植物恢复年限样地土壤理化性质及微生物进行调查测定，分析植物恢复对稀土矿堆浸废弃地土壤理化特性及微生物的影响.结果表明：在植被恢复第3a和4a土壤理化性质显著高于未治理废弃地，但仍显著低于矿区周边未开采对照（P<0.05）.植被恢复年4a以后，长汀稀土矿废弃地土壤理化性质则呈下降趋势，但仍显著高于未治理废弃地（P<0.05）.长汀稀土矿堆浸废弃地不同植被恢复年限土壤细菌丰度及多样存在一定差异.随植被恢复年限的增加，土壤细菌多样性及丰度降低，但一些特殊细菌群如γ-变形菌纲（Gammaproteobacteria）、a-变形杆菌纲（Alphaproteobacteria）、酸杆菌门（Acidobacteria）、蓝藻菌门（Cyanobacteria）等在不同植被恢复年限样地中其相对丰度明显增加.具有固氮作用的蓝藻菌门（Cyanobacteria）随着植被恢复年限的增加，其相对丰度降低.广古菌门（Euryarchaeota）仅存在于未开采对照样地；土壤寡营养细菌酸杆菌门（Acidobacteria）随植被恢复年限的增加，相对丰度呈增大趋势.土壤中优势菌群广古菌门（Euryarchaeota）、厚壁菌门（Firmicutes）、β-变形菌门（Proteobacteria）、Methanobacterium属、罗尔斯通菌属（Ralstonia）与土壤pH、全磷、全钾、速效磷等呈正相关.土壤pH值、全磷、全钾等是影响广古菌门（Euryarchaeota）、厚壁菌门（Firmicutes）等细菌菌群多样性及相对丰度变化的重要因素.以上结果表明，离子型稀土矿堆浸废弃地植被恢复治理到3~4a时，应采取防治措施对其进行人工抚育管理，否则可能会出现前期恢复后期退化的问题.     

Influence of surfactant-facilitated interfacial tension reduction on chlorinated solvent migration in porous media: observations and numerical simulation

The ability of a multiphase flow model to capture the migration behavior of chlorinated solvents under conditions of surfactant-facilitated interfacial tension (IFT) reduction is assessed through comparison of model predictions with observations from controlled laboratory experiments. Tetrachloroethene (PCE) was released in two-dimensional saturated systems, packed with sandy media that incorporated rectangular lenses of capillary contrast. Spatially uniform interfacial tension conditions were created in the tanks by pre-flushing the porous medium with either Milli Q water or an aqueous surfactant solution. Experimental observations showed that surfactant-facilitated IFT reductions substantially lowered capillary resistance to the vertical downward migration of PCE and enabled PCE to enter finer grained, less permeable lenses that were not penetrated in the absence of surfactant. An immiscible flow model was used to simulate the conditions of the laboratory experiments. Under higher IFT conditions (47.5 and 5 dyn/cm), the model could successfully predict the general migration behavior of the organic liquid. Model predictions, however, exhibited poorer agreement with observed migration pathways under low IFT conditions (0.5 dyn/cm). In all cases, the predicted PCE distributions were influenced by selection of the parametric model for capillary retention and relative permeability. Simulated migration rates were more consistent with observed behavior when the Brooks-Corey/Burdine model was employed. For low interfacial tensions, improved predictions of migration pathways were obtained through grid refinement and incorporation of small-scale packing variability. Simulations highlight the substantial sensitivity of model predictions to the capillary pressure-scaling factor, grid resolution, and small-scale porosity variations at interfaces of permeability contrast under reduced IFT conditions.     

连续式离子分离系统(ISEP)在水杨酸生产废水处理中的应用

采用连续式离子分离系统 (ISEP)处理水杨酸生产废水 ,结果表明 ,该系统对水杨酸生产废水有良好的处理效果。当进水CODCr为 180 0 0— 2 0 0 0 0mg/L时 ,经一步吸附处理 ,出水CODCr可实现达标排放 ,苯酚、水杨酸去除率接近10 0 % ,脱附液中高浓度苯酚、水杨酸等资源可有效回收利用     

Simple screening models of NAPL dissolution in the subsurface

Three simple screening models of nonaqueous phase liquid (NAPL) dissolution in the subsurface are proposed based on the NAPL mass conservation and the assumption of proportionality between the residual NAPL source zone concentration and the remaining residual NAPL mass. The purpose of the proposed models is to predict the solute concentration in the zone of the residual NAPL as a result of dissolution. The predicted source zone concentration decrease is used to simulate and account for the decrease of dissolution rate with time. The proposed simple NAPL dissolution models enable the pseudo-equilibrium formulation to be used and therefore the numerical simulations for field application problems can be simplified compared to the non-equilibrium counterpart. With proper choice of empirical parameters, the proposed simple screening models can work as well as more complex dissolution rate correlation models, such as that of Imhoff et al. [Water Resour. Res. 30 (1994) 307-320]. It is found that the proposed models are very good for quantifying non-equilibrium dissolution, which is characterized by tailing of breakthrough curves. The models are especially useful for situations of small residual NAPL saturation, which are typical for many field applications.     

A pore-scale investigation of mass transport from dissolving DNAPL droplets

Spheres and pendular rings of trichloroethylene and tetrachloroethylene are observed dissolving in an artificial porous medium consisting of a single layer of glass beads. Given the simple geometry of the droplets, pore-scale mass transfer coefficients are calculated. For dissolving spheres, mass transfer coefficients are found to be constant over time. However, coefficients for pendular rings are found to decrease as the rings shrink in size. This is consistent with the concept of diffusion-controlled mass transfer in low-flow zones. Sherwood numbers measured at Reynolds numbers between 0.0033 and 8.33 show a similar trend to empirical relationships established by previous researchers using other techniques. As in previous experiments, considerable scatter in mass transfer rates is observed at a given mean flux. It is hypothesized that this variation in local mass transfer rates is caused by variations in local pore velocity.     

Infiltration and redistribution of LNAPL into unsaturated layered porous media

Enhanced understanding of light non-aqueous phase liquid (LNAPL) infiltration into heterogeneous porous media is important for the effective design of remediation strategies. We used a 2-D experimental facility that allows for visual observation of LNAPL contours in order to study LNAPL redistribution in a layered porous medium. The layers are situated in the unsaturated zone near the watertable and they are inclined to be able to observe the effect of discontinuities in capillary forces and relative permeabilities. Two experiments were performed. The first experiment consisted of LNAPL infiltration into a fine sand matrix with a coarse sand layer, and the second experiment consisted of a coarse sand matrix and a fine sand layer. The numerical multi-phase flow model STOMP was validated with regard to the experimental results. This model is able to adequately reproduce the experimental LNAPL contours. Numerical sensitivity analysis was also performed. The capillarity contrast between sands was found to be the main controlling factor determining the final LNAPL distribution.