改良倒置A2/O工艺设计

在目前广泛采用的AO、A2O、倒置A2O等工艺的基础上,为提高脱氮除磷效率,提出改良倒置A2O工艺。并对其工艺的特点、设计和脱氮除磷效率进行了详细的研究和分析。     

节能型虹吸式滗水器的设计与应用

详细介绍了虹吸式滗水器的构成、特点及工作原理,结合理论和实践经验给出了虹吸式滗水器的设计、计算方法及关键设计参数,提出了常规使用方法,整套设备的设计全面而简单明了。     

PCR-DGGE技术分析倒置A~2/O工艺处理染织废水中的微生物区系

基于16S rDNA的PCR-DGGE(polymerase chain reaction-denaturing gradient gel electrophoresis)技术研究了倒置A2/O(anoxic-anaerobic-aerobic)工艺处理染织废水过程中的微生物群落结构.从兼氧、厌氧和好氧区共取6个不同处理阶段的样品,测量了不同处理阶段样品的COD、pH、NH4+-N、H2S、总磷(TP)、污泥含量(TS)、色度及其脱除率,并分析了这些指标的变化规律.结果显示,COD在处理后期降到了145mg·L-1,NH4+-N的脱除率可达到85%,硫化氢的去除率达到了90%以上,磷的脱除率可达80%以上,TS处于逐渐升高的趋势,色度的脱除率达到65%.DGGE图谱显示,好氧处理阶段的微生物多样性明显比兼氧处理和厌氧处理的阶段的要丰富.     

超音速虹吸式空气雾化喷嘴雾化影响因素实验研究

为掌握超音速虹吸式空气雾化喷嘴雾化机理及特性,采用流体力学线性不稳定理论分析雾化机理,通过喷雾实验研究不同因素对雾化性能的影响及对比不同类型喷嘴的雾化效果。研究结果表明：随着距喷嘴出口距离增加,超音速虹吸式空气雾化喷嘴在雾滴破碎后碰撞聚合作用由强到弱,300 mm内雾滴粒径增长速率明显,300 mm外雾滴粒径增长速率较缓。随着供气压力增加,超音速虹吸式空气雾化喷嘴雾滴粒径逐渐减小,在实测距离内SMD(平均粒径)最小为17.5μm。不同供气压力下,超音速虹吸式空气雾化喷嘴随距离增加,雾滴粒径增长趋势基本一致。有效射程内供气压力为0.1～0.5 MPa时,SMD仅为17.5～31.16μm。对比实验中,超音速虹吸式空气雾化喷嘴SMD比内混式空气雾化喷嘴和X旋流型压力喷嘴小53.5%～74.0%。     

A2/O与倒置A2/O工艺低温条件下的氨氮去除能力解析

对相同进水、平行运行的A²/O与倒置A²/O工艺的冬季氨氮（NH₄⁺-N）去除能力进行了全面解析.在运行水温为14℃时,倒置A²/O工艺表现出更低的NH₄⁺-N容积去除负荷［0.13 kg·（m³·d）^-1和0.29 kg·（m³·d）^-1］和氨氧化速率（AOR）［0.07 kg·（kg·d）^-1和0.11 kg·（kg·d）^-1］,而26℃时两个工艺则相差无几.两个平行工艺中的氨氧化菌（AOB）种群定量结果几乎始终相等（倒置A²/O工艺为3.2%±0.24%,A²/O工艺为3.4%±0.31%）.克隆文库分析的结果表明,造成低温时倒置A²/O工艺中具有较低氨氮去除能力的原因是其AOB优势种属为AOR较慢的慢生型（K-生长策略）亚硝化螺菌属（Nitrosospira）,而在A²/O工艺中则为AOR较快的快生型（r-生长策略）亚硝化单胞菌属（Nitrosomonas）;而在26℃环境下两个工艺中的优势种属则均为Nitrosomonas.结合对污染物沿程去除过程的全面分析,发现尽管温度是决定AOB优势种属演替的首要原因,但由于倒置A²/O的工艺结构变化造成其好氧单元具有较高的COD负荷和高NH₄⁺-N浓度等不利于AOB生长的因素,决定了其可以在常规城市污水的条件下出现K-生长策略型的优势AOB种属.因此倒置A²/O针对异养菌（聚磷菌与反硝化菌）的工艺构造变化却通过COD负荷等间接影响到自养型氨氧化菌的种群分布与演替,并最终造成工艺在低温条件下硝化能力的减弱.     

Relationship between filtration activity and food availability in the Mediterranean mussel <Emphasis Type="Italic">Mytilus galloprovincialis</Emphasis>

The filtration activity of the Mediterranean mussel, Mytilus galloprovincialis, was assessed under different concentrations and compositions of seston by using a new automated image acquisition and analysis system. This approach allowed for frequent and simultaneous measurements of valve gape and exhalant siphon area. Filtration rates were measured through clearance measurements whereas pumping rates were measured using hot-film probes. The average filtration rate (17.5 l g h⁻¹ DW⁻¹ for a 0.36 g DW mussel) recorded during the present study was higher than those available for Mytilus edulis when standardized to flesh dry weight but almost equivalent (17.5 l h⁻¹ g DW⁻¹ for a 53 mm shell length mussel) to those rates when standardized to shell length. Immediately after the addition of algal cells (Isochrysis galbana; 4.5 μm in size), valve gape, exhalant siphon area and filtration rate increased quickly as mussels reached their maximum filtration activity. These three parameters then gradually decreased until complete closure of the shell. The algal cell concentration inducing this transition was close to 800 cells ml⁻¹ and 0.5 μg Chl a l⁻¹. When algal concentration was maintained above this threshold by successive algal additions, both valve gape and exhalant siphon area remained maximal. Temporal changes in the exhalant siphon area were continuous as opposed to those of valve gape. Therefore, despite the significant correlation between these two parameters, valves and siphon were sometimes dissociated due to a reduction of the area or even a closure of the exhalant siphon while the valves remained open. The velocity of exhaled water tended to be constant irrespective of exhalant siphon area and thus pumping rates were a linear function of exhalant siphon area. Consequently, reductions in exhalant siphon area and pumping rate were almost similar in M. galloprovincialis. Our results thus clearly support the hypothesis that exhalant siphon area constitutes a better proxy of pumping rate than valve gape as already suggested for Mytilus edulis. Finally, the high filtration rates measured during the present study together with the high concentrations of inorganic matter (> 40 mg DW l⁻¹) requested to alter those rates suggest that the studied mussels were well adapted to oligotrophic waters featuring strong hydrodynamism and frequent sediment resuspension events.     

Designing environmental monitoring networks to measure extremes

This paper discusses challenges arising in the design of networks for monitoring extreme values over the domain of a random environmental space-time field {X _ij } i = 1, . . . , I denoting site and j = 1, . . . denoting time (e.g. hour). The field of extremes for time span r over site domain i = 1, . . . ,I is given by \(\{Y_{i(r+1)}=\max_{j=k}^{k+n-1} X_{ij}\}\) for k = 1 + rn, r = 0, . . . ,. Such networks must not only measure extremes at the monitored sites but also enable their prediction at the non-monitored ones. Designing such a network poses special challenges that do not seem to have been generally recognized. One of these problems is the loss of spatial dependence between site responses in going from the environmental process to the field of extremes it generates. In particular we show empirically that the intersite covariance Cov(Y _i(r+1),Y _i′(r+1)) can generally decline toward zero as r increases, for site pairs i ≠ i′. Thus the measured extreme values may not predict the unmeasured ones very precisely. Consequently high levels of pollution exposure of a sensitive group (e.g. school children) located between monitored sites may be overlooked. This potential deficiency raises concerns about the adequacy of air pollution monitoring networks whose primary role is the detection of noncompliance with air quality standards based on extremes designed to protect human health. The need to monitor for noncompliance and thereby protect human health, points to other issues. How well do networks designed to monitor the field monitor their fields of extremes? What criterion should be used to select prospective monitoring sites when setting up or adding to a network? As the paper demonstrates by assessing an existing network, the answer to the first question is not well, at least in the case considered. To the second, the paper suggests a variety of plausible answers but shows through a simulation study, that they can lead to different optimum designs. The paper offers an approach that circumvents the dilemma posed by the answer to the second question. That approach models the field of extremes (suitably transformed) by a multivariate Gaussian-Inverse Wishart hierarchical Bayesian distribution. The adequacy of this model is empirically assessed in an application by finding the relative coverage frequency of the predictive credibility ellipsoid implied by its posterior distribution. The favorable results obtained suggest this posterior adequately describes that (transformed) field. Hence it can form the basis for designing an appropriate network. Its use is demonstrated by a hypothetical extension of an existing monitoring network. That foundation in turn enables a network to be designed of sufficient density (relative to cost) to serve its regulatory purpose.     

势能增氧生物处理工艺的应用研究

介绍势能增氧生态床的增氧机理及工程实例。生态床为多层浅床结构,每层装设填料,采用虹吸管进出水,利用水流势能进行大气复氧,水中DO逐层增加,出水DO达到最高。结构紧凑,投资省,高效节能,可用于小区中水回用处理,经济效益优于传统工艺。     

松软煤层锚固孔孔底扩孔锚固性能试验研究

针对松软煤层巷道锚杆锚固力低成为制约松软煤层巷道锚杆支护技术发展的瓶颈,提出锚固孔孔底倒楔形扩孔提高锚杆锚固性能的方法,研发了锚固孔孔底单翼扩孔装置,并进行了实验室和井下现场试验,结果表明单翼锚固孔孔底扩孔装置设计的科学性和可行性。通过实验室试验及井下试验得出,锚固孔孔底倒楔形锚固,锚杆的锚固性能至少提高1倍以上,为松软煤层巷道锚杆支护的应用奠定了基础。     

工业用水与经济发展的关系——用水库兹涅茨曲线

经验数据显示,发达国家工业用水随经济发展的变化存在着一个由上升转而下降的转折点。因此,工业用水随收入增长的演变模式可以用库兹涅茨曲线形式来表示。工业用水下降点对应的人均GDP的阈值是3700-17 000US$(PPP,以1985年为基数)。与之相应的第二产业在GDP总量中所占份额是30％～50％。工业用水下降的直接原因是用水效率的提高,其来源有两方面:部门用水效率的提高和经济结构调整。这提供了一个积极的信号,即发展中国家的工业用水将不会一直持续增长,从而为更好地预测发展中国家的工业用水量提供非常重要的思路,也为正确把握用水变化规律,制定符合规律的水资源对策提供科学基础。