电絮凝处理黄土塬地区村镇集蓄雨水的实验研究

采用电凝聚对黄土塬地区村镇集蓄雨水进行处理。通过改变极板间距、极板电压、电解时间,进行了对集雨水中COD,浊度,NH3-N,UV254的去除率研究。结果表明：电解时间15 min,极板间距为10 mm,极板电压为15 V的条件下,电絮凝对集蓄雨水中浊度、氨氮、UV254、COD有较好的去除效果,去除率分别为95%、63%、48%、80%,高于化学絮凝的处理效果。     

The association of E. coli and soil particles in overland flow.

The removal of E. coli from overland flow under saturation-excess runoff conditions was investigated in experimental field plots that were 1 m wide and 5 m long. Variation in the attenuation of bacteria and distance transported was quantified under contrasting flow conditions. In addition, the impact of soil tillage upon microbial attenuation was examined by comparing results derived from grassed plots (intact) with those subject to tillage with the soil left bare (cultivated). For intact plots subjected to a flow of 2 L/min, 27% of the E. coli in the flow was removed after 5 m with removal following a logarithmic function with respect to distance. For the higher flow rates of 6 L/min and 20 L/min, no attenuation trend was observed over this distance. E. coli removal during flow across the cultivated plots was significantly greater compared to the intact plots. This was attributed to a greater infiltration rate in the cultivated plots (due to the tillage) which promoted a greater volume of flow to pass through the soil matrix, providing the opportunity for filtration and adsorption of microbes. Logarithmic trends with respect to distance were observed for all flow rates tested on the cultivated plots (2, 6 and 20 L/min). Total removal after 5 m at a flow rate of 2 L/min was 41% and again removal efficiency decreased as the flow rate increased. Analysis of the transported state of the E. coli revealed that the bacteria were being transported predominantly in particles less than 20 microm in diameter and were not attached to large (dense) soil particles. The limited removal (< 50%) of bacteria from overland flow under saturation-excess runoff conditions in these experiments appeared, therefore, to be primarily due to a lack of settling or deposition. Instead, most bacteria remained entrained within the overland flow down the length of the plots.     

Use of electrochemical oxidation process as post-treatment for the effluents of a UASB reactor treating cellulose pulp mill wastewater.

The main purpose of this study was to evaluate the performance of the electrochemical oxidation process as a post-treatment for the effluents of a bench-scale UASB reactor treating simulated wastewater from an unbleached pulp plant. The oxidation process was performed using a single compartment cell with two plates as electrodes. The anode was made of Ti/Ru0.3Ti0.7O2 and the cathode of stainless steel. The following variables were evaluated: current density (75, 150 and 225 mA cm(-2)) and recirculation flow rate in the electrochemical cell (0.22, 0.45 and 0.90 L h(-1)). The increase in current density from 75 to 225 mA cm(-2) did not increased the color removal efficiency for the tested flow rates, 0.22, 0.45 and 0.90 L h(-1), however the energy consumption increased significantly. The results indicated the technical feasibility of the electrochemical treatment as post-treatment for UASB reactors treating wastewaters from pulp and paper plants.     

New compact scrubber for odour removal in wastewater treatment plants.

This work presents the performances of a new odour scrubber. The reactor is packed with a new structure which enables co-current operations at high gas velocities. Energy consumption and removal efficiency of sulphur compounds by oxidative alkaline scrubbing were studied. The influence of both superficial gas (U(SG)) and liquid (U(SL)) velocities, ranging from 5.6 to 28 m.s(-1) and 0.016 to 0.055 m.s(-1) respectively, were quantified. Thus, the range of 0.5 to 5 liquid-to-gas mass ratio (L/G) was studied. A comparison has been made with a previous study on static mixers (SM) and with classical random packed towers (PT). It has been shown that superficial liquid and gas velocities have a significant influence on these parameters. Hydrogen sulphide (H2S) abatement reached values up to 99%. As concerns methylmercaptan (CH3SH), the maximal removal efficiency was 87%. As a result, if well scaled-up, our reactor can be a small single stage efficient apparatus for the elimination of low concentrations of sulphur compounds as H2S and CH3SH in high flow rates of polluted gas effluents.     

Density‐driven water circulation in a typical tributary of the Three Gorges Reservoir,China

A 2‐D hydrodynamic model was developed for modelling water circulation from 2008 to 2011 in a typical tributary of the Three Gorges Reservoir. The model is capable of describing flow behaviour and mixing mechanisms for different density current patterns and performs well in computing the velocity, the intrusion layer at the plunge point, and the travel distance of the density current. The effects of 10 flow patterns on thermal stratification, hydrodynamics, and algal bloom risk are discussed and classified in terms of algal growth. Patterns (6) and (10) can effectively prevent algal blooms; Patterns (7) and (8) are good for algal blooms. More frequent transformations of flow‐driven patterns, as observed in 2010–2011, could create more eddies and mixing and thus reduce bloom risk. Further studies are necessary and recommended for more accurate predictions, assessing the impact of water level fluctuations on transform flow patterns and water quality.     

小型间歇式次氯酸钠发生器的设计参数研究

为提高小型间歇式次氯酸钠发生器的适用性和可靠性,综合考虑农村小型供水工程特点,结合两端式板式电极,采用单因子试验方法开展电极结构、阴极材质、电极安装高度、盐水浓度、配盐水质、盐水体积、电流密度等设计参数的试验研究。试验结果表明: 小型间歇式次氯酸钠发生器的最佳设计参数为: 电极左右间距 6 cm,阴、阳极采用相同涂层,电极板间距 5 mm,电极板中心距电解槽底部 20 cm,盐水浓度3% ,盐水体积30 L,电流密度480 ～ 640 A /m2,电解时间300 ～ 360 min,有效氯浓度 8. 50 ～ 8. 80 g /L,有效氯产量 255 ～ 264 g,运行成本 7. 16 ～ 7. 20 元/ kg。此外,亦可结合实际供水工程规模、消毒剂需求量、电解时间等多个因素,选择适宜的电解参数。试验结果为下一步设备定型和实际应用奠定了良好基础。     

基于CCHE的重力沉砂池结构布置参数比选研究

为了提高重力沉砂池水沙分离效率,对重力沉砂池相关结构参数进行优化使各项结构参数取得较优值,并研究了侧向溢流堰长度与位置对重力沉砂池最终水沙分离效率的影响,且取得较优的侧堰长度与位置。基于CCHE软件采用混合掺长紊流模型建立CCHE2D重力沉砂池数学模型,得到重力沉砂池内水流流速、泥沙沿程分布及最终水沙分离效率,在已有研究成果基础上分析得到较优的重力沉砂池侧向溢流堰长度及位置。研究结果表明:改变侧向溢流堰长度及位置可将传统重力沉砂池水沙分离效率显著提高。当溢流堰长度取4 m并向上游移动1 m时可将水沙分离效率提高至71.20%。当侧向溢流堰向上游移动一段距离可以阻挡由沉砂池末端产生回流、漩涡等流态而卷起的泥沙,避免其流向清水池,从而提高重力沉砂池水沙分离效率。移动距离不可过前,否则距离过于靠前由于沉砂池边壁的阻挡容易使沉砂池末端形成一段"死水区",使沉砂池有效沉降距离减少,从而降低重力沉砂池水沙分离效率。     

低渗透油藏中水平井两相渗流分析

大量实验表明，在低渗透多孔介质中，渗流不再符合线性达西定律，而具有启动压力梯度，本文从Buckley-Leverret不混溶两相渗流驱替理论出发，考虑启动压力梯度的影响，对水平井两相渗流进行分析，得到了椭球形边水油藏中水平井定产时的压力分布公式和定压生产时的产量公式，以及饱和度分布公式。经图示分析得出结论：启动压力梯度不仅增大油藏的生产压差，而且使油藏的无水采收率和水驱采收率减少；增大注入量可以降低启动压力梯度对两相渗流的不利影响，从而提高水驱采收率，因此开发含启动压力梯度油藏，应小井距，大流量，大压差进行注水开发；水平井的两相渗流解析解为数值模拟中水平井的处理提供很好的方法。     

Emission of greenhouse gases from constructed wetlands for wastewater treatment and from riparian buffer zones.

We measured N2O, CH4 and CO2 fluxes in horizontal and vertical flow constructed wetlands (CW) and in a riparian alder stand in southern Estonia using the closed chamber method in the period from October 2001 to November 2003. The average rates of N20, CH4 and CO2 emission from the riparian gray alder stand were from -0.4 to 58 microg N2O-N m(-2) h(-1) and 0.1-265 microg CH4-C m(-2) h(-1), 55-61 mg CO2-C m(-2) h(-1), respectively. The average N2O-N emission from the microsites above the inflow pipes of horizontal subsurface flow (HSSF) CWs was 6.4-31 microg N2O-N m(-2) h(-1), whereas the outflow microsites emitted 2.4-8 microg N2O-N m(-2) h(-1). In vertical subsurface flow (VSSF) beds the same value was 35.6-44.7 microg N2O-N m(-2) h(-1). The average CH4 emission from the inflow and outflow microsites in the HSSF CWs differed significantly ranging from 640 to 9715 and from 30 to 770 microg CH4-C m(-2) h(-1), respectively. The average CO2 emission was somewhat higher in VSSF beds (140-291 mg CO2-C m(-2) h(-1)) and at inflow microsites of HSSF beds (61-140 mg CO2-C m(-2) h(-1)). The global warming potential (GWP) from N2O and CH4 was comparatively high in both types of CWs (4.8 +/- 9.8 and 6.8 +/- 16.2 t CO2 eq ha(-1) a(-1) in the HSSF CW 6.5 +/- 13.0 and 5.3 +/- 24.7 t CO2 eq ha(-1) a(-1) in the hybrid CW, respectively). The GWP of riparian alder forest from both N2O and CH4 was relatively low (0.4 +/- 1.0 and 0.1 +/- 0.30 t CO2 eq ha(-1) a(-1), respectively), whereas the CO2-C flux was remarkable (3.5 +/- 3.7 t ha(-1) a(-1). The global influence of CWs is not significant. Even if all the global domestic wastewater were treated by wetlands, their share in the trace gas emission budget would be less than 1%.     

Slag columns for upgrading phosphorus removal from constructed wetland effluents.

The current best option to upgrade constructed wetlands (CWs) for phosphorus (P) retention, in terms of efficiency, cost and simplicity, consists in using media having a strong P affinity. The media can be used either in the planted beds or in a filtration system downstream of the beds. The use of slag filters was shown to be efficient for removing P from wastewater as it represented a slow release source of calcium and hydroxide, favouring the formation of hydroxyapatite. Our study aimed at maximising the P retention capacity of slag filters located at the outlet of CWs since electric arc furnace slag has been shown to inhibit the growth of macrophytes when used in the filtration matrix. Bench-scale columns (Vtot = 6.2 L) filled with various combinations of filter media (slag, granite, limestone) of different sizes (2-5, 5-10, 10-20 mm) were fed on-site during four months with a CW effluent (in mg/L: 30 COD, 30 TSS, 10 Pt). Results showed that the best media combination enabling the maximum o-PO4 retention (more than 80% removal without clogging) consisted in a series of a ternary mix column (slag 5-10 mm, granite 2-5 mm, limestone 5-10 mm) followed by a slag column (slag 5-10 mm). Pilot scale columns (Vtot = 300 L), filled with the best media combination, were installed at the outlet of a 28 m2 CW. These columns showed more than 75% removal efficiency during one year and were designed to be easily replaced each year.     

造粒流化床浓缩技术处理给水厂排泥水的中试研究

以南方某给水厂排泥水为处理对象,利用造粒流化床污泥浓缩工艺进行了处理规模为 1-2．5 m3／h的中试研究。研究结果表明,对于排泥水有机物、藻类含量高的南方水厂而言,采用一 体化造粒流化床浓缩工艺进行处理是切实可行的,且具有处理效率高、出泥含水率低、脱水性能好、 出水浊度低等特点;中试条件下,流化床水流上升速度可达38-50 cm／min,最佳搅拌转速为 5 r／min,PAM药耗比普通重力浓缩-调质工艺节省25％-40％,污泥含水率可从99％降至95％- 97％。并通过试验确定了相关工艺参数。     

Removal of E. coli and helminth eggs in UASB: Polishing pond systems in Brazil.

Ponds following anaerobic reactors, such as Upflow Anaerobic Sludge Blanket (UASB) reactors, have been termed polishing ponds in the literature. The present paper analyses the removal of E. coli and helminth eggs in five UASB-polishing pond systems in Brazil. Since there were ponds in series, the total number of ponds was 10. The ponds had average retention times varying from 2 to 21 days, and depths ranging from 0.40 to 2.00 m. The shallow ponds in series, even with low retention times, were able to produce effluents complying with the coliform WHO guidelines for unrestricted irrigation (< or = 1000 MPN/100 ml). An equation for the coliform decay coefficient was proposed: Kb (dispersed flow) = 0.710H(-0955) (20 degrees C). The equation highlights the inverse relationship between the pond depth and the decay coefficient. All polishing pond systems were able to produce effluents with helminth eggs concentrations predominantly equal to zero, and satisfying the WHO guidelines for unrestricted and restricted irrigation (< or = 1 egg/L, arithmetic mean). The approximate range of helminth eggs removal efficiency was predicted satisfactorily.     

双射流流动结构实验研究

应用PIV实验方法对由直射流和同心的环状旋转射流组成的双射流流场进行了测量,并分析研究了流场的速度和旋度变化规律。分析表明,双射流等速核长度较小,仪约为5倍喷距;随喷距的增加其多股射流特性逐渐减弱,其主要原因为直射流和旋转射流在交界面上很强的剪切作用;旋转射流的径向发展因受直射流吸附作用的影响而减小,相应直射流速度在喷嘴轴线上的衰减则增加。在4-6倍喷距间的旋转射流速度突然下降和相应位置处旋度场的涡环都显示该处可能存在较强的空化现象,而大大提升双射流的能力。     

Numerical simulation of hemodynamic interactions of red blood cells in micro-capillary flow

The hemodynamic interactions of red blood cells （RBCs） in a microcapillary flow are investigated in this paper. This kind of interaction is considered as the non-contact mutual interaction of cells, which is important in the suspension flow of blood, but not sufficiently understood. The distributed Lagrange multiplier/fictitious domain method in the lattice Boltzmann framework is used to solve the suspension of the RBCs. The modification of the flow due to the cells, the dependence of the cell deformation on the flow and the cell-cell interaction via the fluid are discussed. It is revealed that the long-range hydrodynamic interaction with a long interacting distance, more than about 5 times of the RBC equivalent radius, mainly has effect on the rheology properties of the suspension, such as the mean velocity, and the short-range interaction is sensitive to the shape of the cell in the microcapillary flow. The flow velocity around the cell plays a key role in the cell deformation. In the current configuration of the flow and cells, the cells repel each other along the capillary.     

Oxygen transfer characteristics of water and bubble mixture pipe flow through two sudden contractions and expansions

The dissolved oxygen （DO） concentration is an important index of water quality. This paper studies the dissolved oxygen recovery of the water and bubble mixture pipe flow through two sudden contractions and expansions. A 3-D computational fluid dy- namics model is established to simulate the water and bubble mixture flow with a DO transport model. An experiment is conducted to validate the mathematical model. The mathematical model is used to evaluate the effect of geometric parameters on the head loss coefficient, the relative saturation coefficient and the oxygen absorption efficiency. It is found that the contraction ratio is a signi- ficant influencing factor, other than the relative length and the relative distance. Given the same relative length and relative distance, the head loss coefficient, the relative saturation coefficient and the oxygen absorption efficiency increase with the decrease of the contraction ratio, respectively. Given the same relative length and contraction ratio, the head loss coefficient increases with the in- crease of the relative distance firstly, and then decreases gradually, in contrast, the relative saturation coefficient and the oxygen ab- sorption efficiency decrease with the increase of the relative distance firstly, and then increase gradually, the relative saturation coefficient and the oxygen absorption efficiency are inversely proportional to the head loss coefficient, respectively.     

水平轴式海流发电装置的设计研究

为了提升海流能发电装置的的能量转换效率,研发了一种水平轴式 S 形叶轮海流发电装 置。采用升力法设计叶轮结构,建立 CATIA 模型并开发了模具,以便于大规模的加工叶轮。设计 了 9 槽 8 极绕组水下防腐永磁发电机,并进行了发电机系统结构的设计。导流罩的线性选择使得 海流速度增加 14% ～ 23% ,但流速过大又造成了装置不稳定。通过工程样机海上试验,验证了永 磁发电机的发电性能,同时检测了发电装置实验阶段的防水及防腐效果。轮机在流速达到 0. 32 m /s 时即实现无负载自起动。在海水流速为 2. 5 m /s 时,轮机的获能功率可达到 1 150 W; 在海水流速为 2 m /s 左右的海况下,轮机的实际获能功率在 900 W 上下,获能效率最高为 32% ,提高了能量的转换 效率。     

Influence of surface layer on hydrology and biology of gravel bed vertical flow constructed wetlands.

In France, gravel vertical flow constructed wetlands (gVFCWs) were adapted to treat raw wastewater, which led to important accumulations of matter in filters (organic and mineral). To prevent clogging, large gravel sizes were employed (O 2-6 mm). The aim of this paper was to present the influences of matter accumulation on the hydraulic and biological behaviour of the system. A one-year survey of accumulated matter content and potential respiration activities was completed in three gVFCWs (operating for 3, 4 and 8 years). Cores were sampled into filters. Results showed a vertical stratification of accumulated matter and respiration rates. Dry accumulated matter quantities ranged from 20 kg m(-2) (3 and 4 years operating) to 80 kg m(-2) in the oldest plant (8 years). Potential respiration was larger in the oldest plant (75g O2m(-2)h(-1)) than in the most recent one (15g O2m(-2)h(-1)). Accumulated matter seemed to play a role both on the water retention (enhancing initial percolation time by 5 times) and biological profile (enhancing microfauna's diversity). Contrary to what is generally proposed in the literature, accumulated matter in French gVFCWs seemed to provide better treatment efficiency without leading to surface clogging compared to systems using sand.     

Operation of a full-scale pumped flow biofilm reactor (PFBR) under two aeration regimes

A novel technology suitable for centralised and decentralised wastewater treatment has been developed, extensively tested at laboratory-scale, and trialled at a number of sites for populations ranging from 15 to 400 population equivalents (PE). The two-reactor-tank pumped flow biofilm reactor (PFBR) is characterised by: (i) its simple construction; (ii) its ease of operation and maintenance; (iii) low operating costs; (iv) low sludge production; and (v) comprising no moving parts or compressors, other than hydraulic pumps. By operating the system in a sequencing batch biofilm reactor (SBBR) mode, the following treatment can be achieved: 5-day biochemical oxygen demand (BOD5), chemical oxygen demand (COD) and total suspended solids (TSS) reduction; nitrification and denitrification. During a 100-day full-scale plant study treating municipal wastewater and operating at 165 PE and 200 PE (Experiments 1 and 2, respectively), maximum average removals of 94% BOD5, 86% TSS and 80% ammonium-nitrogen (NH4-N) were achieved. During the latter part of Experiment 2, effluent concentrations averaged: 14 mg BOD5/l; 32 mg COD(filtered)/l; 14 mg TSS/l; 4.4 mg NH4-N/l; and 4.0 mg NO3-N/l (nitrate-nitrogen). The average energy consumption was 0.46-0.63 kWh/m3(treated) or 1.25-1.76 kWh/kg BOD5 removed. No maintenance was required during these experiments. The PFBR technology offers a low energy, minimal maintenance technology for the treatment of municipal wastewater.     

Efficiency of a turbidity-based, real-time control strategy applied to a retention tank: a simulation study

This paper compares several real-time control (RTC) strategies for a generic configuration consisting of a storage tank with two overflow facilities. Two of the strategies only make use of flow rate data, while the third also introduces turbidity data in order to exercise dynamic control between two overflow locations. The efficiency of each strategy is compared over a wide range of system setups, described by two parameters. This assessment is performed by simulating the application of control strategies to actual measurements time series recorded on two sites. Adding turbidity measurements into an RTC strategy leads to a significant reduction in the annual overflow pollutant load. The pollutant spills spared by such a control strategy strongly depend on the site and on the flow rate based strategy considered as a reference. With the datasets used in this study, values ranging from 5 to 50% were obtained.     

Movements of wild atlantic salmon parr in relation to peaking flows below a hydropower station

Movements of 20 radio‐tagged wild Atlantic salmon (Salmo salar) parr were studied 1.3 km downstream of a hydropower station. Ten parr were free‐ranging and ten were restricted to an area near the river bank by a 75 m² rectangular containment pen that was flooded at high flow, but dry at low flow except for a small refuge at the low end. The positions of contained parr were continuously recorded within a four‐cell uniform grid by continuous data logging, while free‐ranging fish were positioned by manual tracking four times per day. River discharge was manipulated to run five pseudo‐replicated series of three step changes from 30 to 70 to 110 m³ s^?1, with slow (2 h) and rapid (0 h) increase and decrease in discharge, as well as during day and night. No differences in movements or home ranges (mean 2770 m² ± 1759 SD) were detected related to manipulated discharge variations or time of day or night for the free‐ranging parr. No free‐ranging parr were stranded during rapid flow reductions. In the containment pen, the parr distributed themselves relatively evenly among the cells. They moved significantly more at changing than at stable flows. In the containment pen, most of the fish that were stranded were observed during rapid flow reductions at night. Rapid reductions in water flow may cause increased mortality in large parr in shallow habitats if movements are restricted; however, rapid fluctuations did not appear to influence movements or cause stranding by free‐ranging Atlantic salmon parr, which moved considerable distances regardless of discharge. Copyright © 2004 John Wiley & Sons, Ltd.