LNAPLs污染物在层状非均质多孔介质中的运移试验研究

文章通过室内试验研究层状非均质多孔介质中轻非水相液体(Light Non-Aqueous Phase Liquid,LNAPL)的运移机制与分布特性。首先,在二维砂槽上进行LNAPL的入渗试验,试验过程中用数码相机进行拍照,把LANPL的扩散过程以图像的形式记录下来;然后,用AutoCAD对图片进行分析处理,得出不同时刻LNAPL的入渗锋面变化图。结果发现,介质结构突变面改变了LNAPL的迁移模式。在LNAPL由中砂进入细砂层后,由于受到毛细作用的增强,其运移速度加快;而由中砂进入粗砂,受粗砂介质阻滞作用增强的影响,LNAPL运移速度变小。当LNAPL由干砂进入湿润砂体时,由于孔隙水浮托力增大,LNAPL先产生纵向运移,随后以横向迁移的形式在地下水位上部聚积。当达到一定厚度后,LNAPL的压头足以克服浮托力,驱替孔隙水进入砂土孔隙。另外,LNAPL的厚度足够大时,方可克服饱水层受到的浮托力,在地下水位上形成LNAPL池,并因孔隙水向周围砂体排泄,LNAPL池周围的水位上升。     

非均相类Fenton试剂的制备及其在焦化废水处理中的应用研究

利用浸渍法,将Fe3＋负载在经酸碱改性后的粉状活性炭上,当浸渍液浓度为2．5％,固化温度为270℃时,制成的催化剂催化活性较高。用自制的非均相类benton试剂降解焦化废水,通过正交试验和极差分析得出,影响因素的主次顺序为催化剂用量〉初始pH值〉反应时间〉H：0：投加量。结果表明,在100ml水样中。室温条件下,初始pH值为4．0,催化剂使用量为1．5g,H20：投加量为5ml（分两次投加）,反应时间为90min时,COD去除率可达99％。采用混凝＋化学沉淀＋非均相类Fenton试剂法处理焦化废水,各主要出水水质指标为：色度lO倍;COD浓度38．5mg／L;氨氮浓度8．4mg／L,达到国家一级排放标准。     

LNAPL在砂质含水层中动态迁移的电阻率法监测试验研究

在海滨潮间带采集细砂,通过室内柴油泄漏模拟试验,利用自制电阻率监测系统对轻非水相液体在砂土-地下水系统垂向渗透过程进行电阻率变化动态监测;通过配制不同含油率砂土测定其静态电阻率变化规律,探讨电阻率变化的影响因素;最后取样分析测定污染含水介质稳定后含水率及含油率,对监测结果有效性进行了验证;并利用显微成像法对污染砂土进行了微观形态分析.结果表明,柴油污染砂土微观形态上胶结现象明显;柴油渗透海滨砂土过程电阻率大小同含水饱和度,比电阻率和含油饱和度之间存在良好的相关性,均可用Archie公式拟合,n值分别为2.36和0.15;通过电阻率测定可以有效估算柴油透镜体厚度;电阻率随深度的变化可以反映含油率和含水率的垂向分布.本研究为轻质油品储罐或者海上油品输运过程泄露造成的海滨砂土地下污染扩散过程监测及机制研究提供了一种有效的方法,也可为其他典型石油泄漏污染场地的电阻率法探测或监测提供参考.     

TiO2 nanotubes as solid-phase extraction adsorbent for the determination of polycyclic aromatic hydrocarbons in environmental water samples

An analytical method based on TiO2 nanotubes solid-phase extraction (SPE) combined with gas chromatography (GC) was established for the analysis of seven polycyclic aromatic hydrocarbons (PAHs): acenaphtylene, acenaphthene, anthracene, fluorene, phenanthrene, fluoranthene and pyrene. Factors a ecting the extraction e ciency including the eluent type and its volume, adsorbent amount, sample volume, sample pH and sample flow rate were optimized. The characteristic data of analytical performance were determined to investigate the sensitivity and precision of the method. Under the optimized extraction conditions, the method showed good linearity in the range of 0.01–0.8 g/mL, repeatability of the extraction (RSD were between 6.7% and 13.5%, n = 5) and satisfactory detection limits (0.017–0.059 ng/mL). The developed method was successfully applied to the analysis of surface water (tap, river and dam) samples. The recoveries of PAHs spiked in environmental water samples ranged from 90% to 100%. All the results indicated the potential application of titanate nanotubes as solid-phase extraction adsorbents to pre-treat water samples.     

1987-2006年厦门市土地利用变化检测分析

通过对厦门市五个时相的土地利用变化检测,分析了厦门市1987年-2006年间各分区的土地利用变化及各地类在各年间的变化情况,并分析其变化原因.     

静置/好氧/缺氧序批式反应器（SBR）脱氮除磷效果研究

以静置段代替传统厌氧段,采用后置缺氧方式,考察了静置/好氧/缺氧序批式反应器(SBR)(R1)的生物脱氮除磷(BNR)性能,并与传统厌氧/好氧/缺氧序批式反应器(SBR)(R2)进行对比.两反应器进水乙酸钠、氨氮(NH+4-N)及磷酸盐(PO3-4-P)浓度均分别为350 mg·L-1(以COD计)、40 mg·L-1及12 mg·L-1,水力停留时间(HRT)为12 h.研究结果表明,R1长期运行中磷的去除率与R2相当,分别为92.4%和92.1%,而总氮(TN)去除率则较R2高,分别为83.5%和77.0%.R1静置段省去搅拌但仍能起到厌氧段的作用,为好氧快速摄磷奠定了基础,同时R1缺氧段发生反硝化摄磷,使出水磷降至0.91 mg·L-1.好氧段内R1发生了同步硝化-反硝化(SND),贡献了18.0%的TN去除量,R2也存在SND,但脱氮贡献率较少,仅为9.8%.R1和R2后置缺氧反硝化均以糖原驱动,反硝化速率分别为0.98、0.84 mg·g-1·h-1(以每g VSS产生的N(mg)计),出水TN分别为6.62、9.21 mg·L-1.研究表明,静置段代替传统厌氧段后,可获得更好的脱氮效果,且工艺更为简化.     

固相萃取-高效液相色谱法测定水中丙烯酰胺研究

采用固相萃取-高效液相色谱法对水中的丙烯酰胺定性、定量分析。结果显示:丙烯酰胺含量在20μg/L~400μg/L之间呈良好线性关系,回归方程Y=0.476 8X+0.845 4,相关系数R为0.997 72,检出限0.1μg/L,样品回收率在71.85%~92.28%之间,相对标准偏差为3.4%~10.9%。该方法减少了有机溶剂用量,缩短了有机溶剂暴露时间,降低污染,且能满足地表水环境质量标准(GB 3838-2002)限值要求,是水中丙烯酰胺含量准确稳定的检测方法。用该方法测定了呼和浩特市引黄入呼左岸、右岸、中浅和中深4个断面水样,均未检出丙烯酰胺。     

纳米TiO2/CNTs复合材料的制备及其光学性质

TiO2在碳纳米管上的复合材料可以增加材料的光催化性能,已成为新的研究热点.本文采用低温液相法成功地合成了TiO2/CNTs复合材料,并用TEM、XRD和UV-vis对材料进行了表征,结果表明,TiO2很好地分散在CNTs上,具有显著的催化效果,有很好的应用前景.     

喻家土扁滑坡形成的力学机理与险情分析

喻家滑坡发现于去年5月,体积近17×104m3,呈长条纺棰状,分成上.下滑块,本文从斜坡的变形历史、特征调查入手,较深入地研究了该滑坡滑移-拉裂-推动-牵引的耦合力学机理,该滑坡正处在蠕滑阶段,近期存在整体滑移和出现较大危害的险情,已引起有关部门的重视,并采取了有力的减灾防灾措施.     

Effect of soil moisture dynamics on dense nonaqueous phase liquid (DNAPL) spill zone architecture in heterogeneous porous media

The amount, location, and form of NAPL in contaminated vadose zones are controlled by the spatial distribution of water saturation and soil permeability, the NAPL spill scenario, water infiltration events, and vapor transport. To evaluate the effects of these processes, we used the three-phase flow simulator STOMP, which includes a new permeability-liquid saturation-capillary pressure (k-S-P) constitutive model. This new constitutive model considers three NAPL forms: free, residual, and trapped. A 2-D vertical cross-section with five stratigraphic layers was assumed, and simulations were performed for seven cases. The conceptual model of the soil heterogeneity was based upon the stratigraphy at the Hanford carbon tetrachloride (CT) spill site. Some cases considered co-disposal of NAPL with large volumes of wastewater, as also occurred at the Hanford CT site. In these cases, the form and location of NAPL were most strongly influenced by high water discharge rates and NAPL evaporation to the atmosphere. In order to investigate the impact of heterogeneity, the hydraulic conductivity within the lower permeability layer was modeled as a realization of a random field having three different classes. For six extreme cases of 100 realizations, the CT mass that reached the water table varied by a factor of two, and was primarily controlled by the degree of lateral connectivity of the low conductivity class within the lowest permeability layer. The grid size at the top boundary had a dramatic impact on NAPL diffusive flux just after the spill event when the NAPL was present near the ground surface. NAPL evaporation with a fine grid spacing at the top boundary decreased CT mass that reached the water table by 74%, compared to the case with a coarse grid spacing, while barometric pumping had a marginal effect for the case of a continuous NAPL spill scenario considered in this work. For low water infiltration rate scenarios, the distribution of water content prior to a NAPL spill event decreased CT mass that reached the water table by 98% and had a significant impact on the formation of trapped NAPL. For all cases simulated, use of the new constitutive model that allows the formation of residual NAPL increased the amount of NAPL retained in the vadose zone. Density-driven advective gas flow from the ground surface controlled vapor migration in strongly anisotropic layers, causing NAPL mass flux to the lower layer to be reduced. These simulations indicate that consideration of the formation of residual and trapped NAPLs and dynamic boundary conditions (e.g., areas, rates, and periods of different NAPL and water discharge and fluctuations of atmospheric pressure) in the context of full three-phase flow are needed, especially for NAPL spill events at the ground surface. In addition, NAPL evaporation, density-driven gas advection, and NAPL vertical movement enhanced by water flow must be considered in order to predict NAPL distribution and migration in the vadose zone.