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681.
Ren Lefebvre Daryl Hockley Jason Smolensky Ann Lamontagne 《Journal of contaminant hydrology》2001,52(1-4):165-186
Acid mine drainage (AMD) results from the oxidation of sulfides, mainly pyrite, present in mine wastes, either mill tailings or waste rock. This is the second of two papers describing the coupled physical processes taking place in waste rock piles undergoing AMD production. Since the oxidation of pyrite involves the consumption of oxygen and the production of heat, the oxidation process initiates coupled processes of gas transfer by diffusion and convection as well as heat transfer. These processes influence the supply of oxygen that is required to sustain the oxidation process. This second paper describes a numerical simulator used to represent the interaction of these coupled transfer processes. Numerical simulations are applied to two large sites with extensive characterization programs and widely different properties and behavior that were described in the first paper. The South Dump of the Doyon mine in Canada is permeable and has a high pyrite oxidation rate, thus making temperature-driven air convection the main oxygen supply mechanism. The Nordhalde of the Ronnenberg mining district in Germany contains lower permeability material which is less reactive, thus leading to a more balanced contribution of gaseous diffusion and convection as oxygen supply mechanisms. Overall, simulations allow a coherent representation of the conditions monitored within the waste rock piles and the confirmation of their physical properties. Conceptual simulations are also carried out to illustrate the potential effect of border membranes and layered co-mingling as mitigation methods used to control AMD production in either active or future waste rock piles. 相似文献
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以富营养化源水为处理对象,考察了三阶、单阶气水顺流、单阶气水逆流生物膜反应器对微囊藻毒素的去除特性.三阶生物膜反应器比单阶反应器更接近于推流反应器,对藻毒素的去除效率高于单阶反应器,且效果稳定.在试验水质条件下,水力停留时间(HRT)为2h时,三阶反应器可有效去除85.9%的胞外微囊藻毒素与84.0%的总微囊藻毒素,对胞外微囊藻毒素-LR、RR与总微囊藻毒素-LR、RR的去除率分别为86.7%、81.7%与71.5%、80.5%.三阶生物膜工艺可用于富营养化源水的预处理. 相似文献
685.
水流模拟断面中硝基苯的迁移转化规律 总被引:1,自引:0,他引:1
采用实验室模拟装置研究了4,10和20 ℃条件下,封闭、开放状态和不同环境因素影响下硝基苯污染水团流经模拟断面前后, 硝基苯在上覆水与沉积物中的迁移转化规律. 结果表明:封闭、开放状态模拟断面上覆水和沉积物中硝基苯迁移分配受温度变化影响显著;开放状态下,上覆水、沉积物中硝基苯变化量均低于封闭状态. 挥发不但影响硝基苯在沉积物-上覆水间的迁移分配,而且能促进沉积物中硝基苯的解吸;光照对模拟断面硝基苯迁移转化无影响. 对于相同的沉积物和上覆水,影响模拟断面系统中硝基苯迁移、分配的因素依次为温度、挥发和光照. 分析实验结果和材料推测,硝基苯在该实验条件下不存在降解转化. 相似文献
686.
This paper is to show that most discrete models used for population dynamics in ecology are inherently pathological that their predications cannot be independently verified by experiments because they violate a fundamental principle of physics. The result is used to tackle an on-going controversy regarding ecological chaos. Another implication of the result is that all dynamical systems must be modeled by differential equations. As a result it suggests that researches based on discrete modeling must be closely scrutinized and the teaching of calculus and differential equations must be emphasized for students of biology. 相似文献
687.
以从连续流搅拌槽式反应器(CSTR)内的活性污泥中分离出的厌氧产氢菌Ethanologenens sp.ZGX4为出发菌株,经过紫外线和亚硝酸复合诱变,从大量的突变体中筛选出一株稳定的高效产氢菌株RF-9.磷酸盐浓度在120mmol/L、温度37℃、初始pH6.0、葡萄糖浓度10g/L培养条件下,RF-9的单位体积产氢量和氢气产率为139.7mmol/L和2.52mol H2/mol葡萄糖,分别是对照的1.50倍和1.43倍.在发酵时间为15h、pH4.1、细胞干重0.722g/L时,RF-9获得其最大产氢速率345mLH2/(h·L),是对照ZGX4的1.41倍.RF-9的主要液相末端产物为乙醇和乙酸,为典型的乙醇发酵细菌,与对照相似. 相似文献
688.
黄河河口地区生态供水效益分析 总被引:2,自引:0,他引:2
流域生态需水是指流域生态系统为维持一定程度的生态系统健康所需要一定质量的水量,以保证流域生态系统结构和生态功能等为目标,实现流域生态系统健康。流域生态需水量的研究对于社会经济的可持续发展具有重要的战略意义。论文针对南水北调西线一期工程的供水规划,在提出配水效益计算方法的基础上,针对不同的配水量,计算了黄河河口地区的生态需水量、生态效益以及供水对减少断流所带来的生态效益,并进行了方案比较分析。主要结论是:当来水量分别为55×108、122.8×108或240×108m3时,产生的湿地综合生态效益则为34.85×108、47.18×108或54.72×108元。 相似文献
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The majority of experimental tests done on combustible dusts are performed in constant volume vessels that have limited or no optical access. Over the years, McGill University has been developing alternative experimental techniques based on direct observation of dust flames, yielding reliable fundamental parameters such as flame burning velocity, temperature and structure. The present work describes two new experimental set-ups allowing direct observation of isobaric and freely propagating dust flames at two sufficiently different scales to test the influence of scale on dust flame phenomena. In the laboratory-scale experiments, a few grams of aluminum powder are dispersed in transparent, 30 cm diameter latex balloons that allow for full visualization of the spherical flame propagation. In the field experiments, about 1 kg of aluminum powder is dispersed by a short pulse of air, forming a conical dust cloud with a total volume of about 5 m3. High-speed digital imaging is used to record the particle dispersal and flame propagation in both configurations. In the small-scale laboratory tests, the measured flame speed is found to be about 2.0 ± 0.2 m/s in fuel-rich aluminium clouds. The burning velocity, calculated by dividing the measured flame speed by the expansion factor deduced from thermodynamic equilibrium calculations, correlates well with the previously measured burning velocity of about 22–24 cm/s from Bunsen dust flames. Flame speeds observed in field experiments with large-scale clouds, however, are found to be much higher, in the range of 12 ± 2 m/s. Estimations are presented that show that the presumably greater role of radiative heat transfer in larger-scale aluminium flames is insufficient to explain the six-fold increase in flame speed. The role of residual large-eddy turbulence, as well as the frozen-turbulence effect leading to large-scale dust concentration fluctuations that cause flame folding, are discussed as two possible sources for the greater flame speed. 相似文献