水力割缝增透抽采煤层瓦斯原理及应用

煤层瓦斯抽采是避免煤矿瓦斯灾害发生的根本防治措施,水力割缝技术使煤体在割缝后应力松弛、卸压、破坏、破裂,以成倍或者十几倍地提高煤层的渗透性,继而对煤层瓦斯进行抽采,使瓦斯煤层变为低瓦斯或无瓦斯煤层,从根本上避免瓦斯灾害发生。从水力割缝技术切割煤层致煤层应力变化角度,将理论分析和数值模拟方法相结合,根据渗流力学平面径向流理论,分析给出水力割缝技术增透抽采瓦斯原理。以兖州东滩矿3号煤层为例,分析采用水力割缝技术前后煤层应力变化、渗透率变化规律。结果表明:大面积割缝后,应力重新分布,由均匀状态转变为非均匀状态分布,水平缝使煤层卸压,煤层应力普遍降低,在缝上部煤层局部形成拉应力区。割缝后渗透率是割缝前的4.34倍,渗透率大幅度增加,从而提高瓦斯抽采速度和最终抽采率。     

Evaporating liquid flow in a channel (An integral model based on shallow water flow approximation)

Liquefied Natural Gas (LNG) storage facilities generally include channels to convey potential spills of the liquid to an impoundment. There is increasing concern that dispersion of vapors generated by flow of LNG in a channel may lead to higher than limit vapor concentrations for safety at site boundary from channels that may be close to the dike walls. This issue is of recent concern to regulatory agencies, because the calculation of vapor hazard distance(s) from LNG flow in a channel is not required under existing LNG facility siting standards or regulations.An important parameter that directly affects the calculated LNG vapor dispersion distance is the source strength (i.e., the rate of vaporization of LNG flow from the wetted channel surfaces, as a function of spatial position and time). In this paper a model is presented which considers the variation of the depth of the flowing LNG with spatial location and time, and calculates the spatial and temporal dependence of the mass rate of vapor generation. Self similar profiles for the spatial variation of the thermal boundary layer in the liquid wetted wall and liquid depth variation are assumed. The variation with time of the location of the liquid spread front and the evaporation rate are calculated for the case of a constant LNG spill rate into a rectangular channel. The effects of two different channel slopes are evaluated. Details of the results and their impact on dispersion distances are discussed.     

基于CFD对袋式除尘器流场的分析

采用计算流体力学(CFD)软件对袋式除尘器单元气流组织进行数值模拟分析,给出了 沿滤袋高度方向过滤风速的分布,以及袋间隙气流抬升速度在不同高度上的分布特征,为袋式除尘器的改进和设计提供理论依据.     

垂直流人工湿地系统基质优化级配研究

选取生物陶粒、无烟煤、沸石、钢渣和蛭石为基质,按不同的级配方式填充成基质柱,进行垂直流人工湿地模拟柱净化污水实验.研究表明,粒径分层级配基质对COD的去除率均高于单一粒径基质,其中分层生物陶粒对COD的平均去除率高达72.91%.分层沸石对总氮的净化能力较单一粒径基质有所提高,平均去除率高达91.23%.填充了生物陶粒、沸石和无烟煤的模拟柱对有机物和氮的净化效果和单一基质没有显著性差异(p0.05).填充钢渣和无烟煤的模拟柱出水pH值均在正常范围内,但是除从上到下依次填充无烟煤、蛭石和钢渣的基质柱外,其它填充钢渣和无烟煤的模拟柱对磷素的净化能力都低于单一基质.种植植物对净化效果没有明显影响.在垂直流人工湿地中,针对水质特点选择高效的级配基质,如分层生物陶粒、分层沸石、分层无烟煤以及生物陶粒、沸石和无烟煤组合,在高水力负荷条件下可获得更好的处理效果.     

Kinetic-spectrophotometric determination of free cyanide by stopped-flow reversed flow injection analysis

A stopped-flow reversed flow injection method for the determination of free cyanide is proposed. Pyridine-barbituric acid mixture is injected in the flow system as reagent to form the colour species with cyanide. The flow is stopped when the reagent zone comes in the flow cell, where absorbance-time data are collected at 580nm wavelength. The linear range of the determination is 0.1 -10μg/ml CN-. The sampling rate is 60h-1 and the relative standard deviation is 1.6% (n=16) at 5.0 μg/ml CN-1 level. With satisfactory results, the proposed method was applied to the determination of free cyanide in wastewater without sample pretreatment.     

山体对烟羽弥散影响的一种数值模拟方法

本文对山地和丘陵地区中烟羽浓度扩散分布的计算提出一种方法,该方法引用浓度方程的分析解,通过对山地绕流数值计算速度势和流函数,可较简易地求得烟羽浓度分布。作为算例,文中对中条山某工厂烟囟排放的SO2,预测了它在各种风速时被输运扩敢的浓度分布。      

流动注射-分光光度法测定工业废水中的Fe^2＋和Fe^3＋

将Fe^2 与邻菲啰啉的显色反应引入流动注射系统，用盐酸羟胺将Fe^3 预先还原，0～6μg/ml的Fe^2符合比耳定律，检测出限0．11μg／ml。0．25μg／mlFe^2 经5次测定的标准偏差为2．2％，进样频率为120次／h，回收率98．5～104％。对工业废水中铁的测定取得了满意的效果。     

Removal of trace elements in three horizontal sub-surface flow constructed wetlands in the Czech Republic

Between March 2006 and June 2008 removal of 34 trace elements was measured on a monthly basis at three horizontal-flow constructed wetlands in the Czech Republic designed to treat municipal wastewater. In general, the results indicated a very wide range of removal efficiencies among studied elements. The highest degree of removal (average of 90%) was found for aluminum. High average removal was also recorded for zinc (78%). Elements removed in the range of 50-75% were uranium, antimony, copper, lead, molybdenum, chromium, barium, iron and gallium. Removal of cadmium, tin, mercury, silver, selenium and nickel varied between 25 and 50%. Low retention (0-25%) was observed for vanadium, lithium, boron, cobalt and strontium. There were two elements (manganese and arsenic) for which average outflow concentrations were higher compared to inflow concentrations. Reduced manganese compounds are very soluble and therefore they are washed out under anaerobic conditions.     

基于EFDC的长江常州段污水排江浓度场数值模拟

长江感潮河段水流与污染排放引起的浓度场复杂多变,基于EFDC(Environmental Fluid Dynamic Code)模型,采用正交曲线网格拟合自然河道边界,建立了长江常州段的水动力和水质模型。采用现场同步实测资料,与计算结果比对,证明该模型在水动力和水质两个方面都与实测数据吻合较好,满足了实际工程的需要;同时由于长江水流运动较快,一阶降解动力学已经满足了化学需氧量(COD)、氨氮(NH3-N)和总磷(TP)浓度计算要求,可以不考虑它们复杂的生化反应过程。     

浅析河流允许排污量计算的设计流量

对淮河淮南段水污染物允许排放量计算中出现大流量小允许排放量的反常现象进行了讨论,并从河流纳污能力形成机制和排污量计算方程等方面问题的产生原因作了定量剖析,又以淮南市段为实例,对设计流量应如保判别和确定作了初步探讨。