人群密度对人群拥挤事故的影响

为了研究公共场所的人群密度与拥挤事故的发生概率.基于连续人群流动模型,从人群密度角度探讨了人群拥挤事故发生的机理.由于不同民族个体生理尺寸的差异,人群最大忍受密度不同,以此作为判断人群拥挤事故的标准,并结合我国情况提出我国人群最大忍受密度为9人/m2.最后模拟了某个拥挤事故场景,用该模型对其进行拥挤事故分析.结果表明,连续人群流动模型可以用于预测拥挤事故的发生,对预防和控制人群拥挤事故具有一定的指导意义.     

海岸带含水层咸淡水界面随潮汐波动的数值模拟

在分析、研究了滨海地带含水层和不透水层的水文地质特性及含水层内的咸淡水渗流运动特征的基础上,运用数学推理的手法,建立了一种较为简单适用的模拟海岸带含水层咸淡水界面和天然地下水面变动规律的二维数学模型,通过该模型的计算值与实验值的比较,证明该模型的计算结果与实验结果有着非常好的拟合度,即该模型能较客观地揭示海水入侵引起的咸淡水界面的变化规律.其后,运用该模型系统的探讨了含水层以下为非平坦的不透水层的滨海地带天然地下水面、咸淡水界面伴随着潮汐的波动而变化的规律.即伴随着潮汐的波动,一方面天然地下水面和咸淡水界面与潮汐具有相似的振动波形,波动的幅度随离海岸距离的增加而减小.在海岸附近咸淡水界面的振幅大于天然地下水面的振幅,而在离开海岸一定距离后天然地下水面的振幅超过咸淡水界面的振幅.总体上天然地下水面的振幅呈负指数衰减,而咸淡水界面的振幅几乎呈直线衰减(其衰减直线的倾角在135～150 °之间变动),且潮汐波动对天然地下水面影响的范围远大于其对咸淡水界面的影响;另一方面天然地下水面和咸淡水界面波动的振幅及它们之间的相位差的大小还与天然地下水面的水力坡度、含水层的渗透系数、有效孔隙率、不透水层形状及其变动的幅度有关,但它们之间的相位差的大小与潮汐波动的幅度无关,其振幅与潮汐的振幅成比例增减.当不透水层的形状一定时,不论天然地下水面的水力坡度、含水层的渗透系数、有效孔隙率及潮汐波动的幅度怎么变动,天然地下水面、咸淡水界面振动的相位差的变化趋势及其峰值出现的位置几乎不变,即不透水层的形状决定着天然地下水面、咸淡水界面振动的相位差的变化趋势,而其大小与含水层的水文地质参数(水力坡度、渗透系数及有效孔隙率)密切相关.此外,当天然地下水面和咸淡水界面的振动存在相位和振幅的较大差异时,可以断定含水层以下存在非平坦的不透水层,且这种差异越大,不透水层凸凹不平的程度越高.     

Experimental investigation of the e ect of flow turbulence and sediment transport patterns on the adsorption of cadmium ions onto sediment particles

The mechanism of flow turbulence,sediment supply conditions,and sediment transport patterns that affect the adsorption of cadmiumions onto sediment particles in natural waters are experimentally simulated and studied both in batch reactors and in a turbulencesimulation tank.By changing the agitation conditions,the sediment transport in batch reactors can be categorized into bottom sediment-dominated sediment and suspended sediment-dominated sediment.It is found that the adsorption rate of bottom sediment is much lessthan that of suspended sediment,but the sediment transport pattern does not affect the final(equilibrium)concentration of dissolvedcadmium.This result indicates that the parameters of an adsorption isotherm are the same regardless of the sediment transport pattern.Inthe turbulence simulation tank,the turbulence is generated by harmonic grid-stirred motions,and the turbulence intensity is quantifiedin terms of eddy diffusivity,which is equal to 9.84F(F is the harmonic vibration frequency)and is comparable to natural surfacewater conditions.When the turbulence intensity of flow is low and sediment particles stay as bottom sediment,the adsorption rateis significantly low,and the adsorption quantity compared with that of suspended sediment is negligible in the 6 h duration of theexperiment.This result greatly favors the simplification of the numerical modeling of heavy metal pollutant transformation in naturalrivers.When the turbulence intensity is high but bottom sediment persists,the rate and extent of descent of the dissolved cadmiumconcentration in the tank noticeably increase,and the time that is required to reach adsorption equilibrium also increases considerablydue to the continuous exchange that occurs between the suspended sediment and the bottom sediment.A comparison of the results ofthe experiments in the batch reactor and those in the turbulence simulation tank reveals that the adsorption ability of the sediment,andin particular the adsorption rate,is greatly over-estimated in the batch reactor.     

Spatial and temporal variations in groundwater nitrate at an intensive dairy farm in south-east Ireland: Insights from stable isotope data

Achievement of at least “good ecological status” in all waterbodies under the EU Water Framework Directive by 2015 will in some cases be a challenge. The twin challenge is to manage expectations of policy makers for such waterbodies as to a realistic length of time required for improvement in water quality. Hence, understanding the source, transformation processes and residence time of nitrate in a hydrological system is an essential part of meeting such challenges. On a dairy farm with 24 shallow groundwater wells, the dual isotopic composition of nitrate (δ¹⁵N and δ¹⁸O) was used to clarify nitrate sources, to assess spatial and temporal variability in nitrate concentrations and to determine if and where denitrification was occurring. Vertical travel time was estimated to correlate nitrate concentrations with management practices. Organically derived nitrogen was the predominant source contributing to groundwater nitrate concentrations. Denitrification was identified as prevalent within specific regions of the study site. The distinct low temporal variability in the isotopic data suggests constancy among nitrate sources and processes over time across the study site. Vertical travel times of up to 3 years were estimated on site indicating the influence of recent management practices on nitrate concentrations. Very slow horizontal migration of groundwater (decades) indicates a legacy of older management practices. Stable isotope techniques, together with an understanding of time lag, provide an extra mechanism to test the efficacy of monitoring and mitigation programmes.     

基于ARDL方法分析福建省资源利用与经济增长关系

运用物质流分析方法以及最新发展的自回归分布滞后模型(ARDL),对福建省1990~2008年资源利用和实际GDP二者关系进行检验和分析.采用了物质流分析指标中直接物质投入来表征区域资源利用量.ARDL边界检验结果表明,资源利用和经济增长间存在稳定的长期均衡关系.进一步通过ARDL模型揭示了区域经济增长对资源利用长期弹性系数,其值约为0.73,通过误差修正模型揭示了短期弹性系数,表明了经济增长到资源利用的长期格兰杰因果关系.对福建省经济增长和资源保护战略提出了政策建议.这一研究思路和方法具有普适性,可以适用于其他地区关于资源利用和经济增长的问题的讨论和研究.     

连续流动氢化物发生原子荧光法测定水中硒

文章介绍连续流动一氢化物发生一原子荧光测定水中硒的方法,研究了盐酸浓度、硼氢化钾浓度、灯电流、光电倍增管负高压、泵速、载气和屏蔽气流量等对测定硒的影响,找出测定水中硒最佳条件,在最佳条件下,校准曲线相关系数为0.9999.方法检出限为0.0095μg/L,方法的测量范围为0.038-300μg/L,回收率在91.8%-...     

扬水曝气器曝气室提水性能模型应用研究

文章根据扬水曝气器曝气室的流体特性,在曝气室内气-液两相流体所受推动力和曳力平衡条件下,建立了一维两相流提水性能模型,并应用于同温层曝气器流体运动特性的模拟预测。结果表明:模型对同温层曝气器上升段气含率的估计值与实测值之间的误差限为±10%,对流体表观上升速度的误差限为±20%。这说明提水性能模型对同温层曝气器的流体特性模拟具有很强的适用性。     

有关斜管沉淀池的上升流速讨论

文章从理论上了分析斜管沉淀池上升流速对沉淀池处理效果的影响,及原水特性与斜管沉淀池上升流速取值的关系。讨论分析斜管沉淀池设计时,应根据原水特性不同选择不同的斜管沉淀池上升流速。     

Efficient dechlorination of chlorinated solvent pollutants under UV irradiation by using the synthesized TiO2 nano-sheets in aqueous phase

Titanium dioxide(TiO2), which is the widely used photo-catalyst, has been synthesized by simple hydrothermal solution containing tetrabutyl titanate and hydrofluoric acid. The synthesized product has been applied to photo-degradation in aqueous phase of chlorinated solvents, namely tetrachloroethene(PCE), trichloroethene(TCE) and 1,1,1-trichloroethane(TCA). The photo-degradation results revealed that the degradation of these harmful chemicals was better in UV/synthesized TiO2 system compared to UV/commercial P25 system and UV only system. The photo-catalytic efficiency of the synthesized TiO2 was 1.4, 1.8 and 3.0 folds higher compared to the commercial P25 for TCA, TCE and PCE degradation, respectively. Moreover, using nitrobenzene(NB) as a probe of hydroxyl radical(.OH), the degradation rate was better over UV/synthesized TiO2, suggesting the high concentration of.OH generated in UV/synthesized TiO2system. In addition,.OH concentration was confirmed by the strong peak displayed in EPR analysis over UV/synthesized TiO2system. The characterization result using XRD and TEM showed that the synthesized TiO2 was in anatase form and consisted of well-defined sheet-shaped structures having a rectangular outline with a thickness of 4 nm, side length of 50 nm and width of 33 nm and a surface 90.3 m2/g. XPS analysis revealed that ≡Ti-F bond was formed on the surface of the synthesized TiO2. The above results on both photocatalytic activity and the surface analysis demonstrated the good applicability of the synthesized TiO2 nano-sheets for the remediation of chlorinated solvent contaminated groundwater.     

Fouling distribution in forward osmosis membrane process

Fouling behavior along the length of membrane module was systematically investigated by performing simple modeling and lab-scale experiments of forward osmosis （FO） membrane process. The flux distribution model developed in this study showed a good agreement with experimental results, validating the robustness of the model. This model demonstrated, as expected, that the permeate flux decreased along the membrane channel due to decreasing osmotic pressure differential across the FO membrane. A series of fouling experiments were conducted under the draw and feed solutions at various recoveries simulated by the model. The simulated fouling experiments revealed that higher organic （alginate） fouling and thus more flux decline were observed at the last section of a membrane channel, as foulants in feed solution became more concentrated. Furthermore, the water flux in FO process declined more severely as the recovery increased due to more foulants transported to membrane surface with elevated solute concentrations at higher recovery, which created favorable solution environments for organic adsorption. The fouling reversibility also decreased at the last section of the membrane channel, suggesting that fouling distribution on FO membrane along the module should be carefully examined to improve overall cleaning efficiency. Lastly, it was found that such fouling distribution observed with co-current flow operation became less pronounced in counter- current flow operation of FO membrane process.