车库内氢气扩散和分布状态的数值模拟

为研究车库内氢气连续性泄漏的浓度分布和聚集状态,采用ICEM-CFD软件建模,利用Fluent软件对氢气连续性泄漏过程进行了模拟。通过分析监测点氢气物质的量分数、氢气分布和可燃性区域体积分数,研究了横梁及其间距(L)、自然通风、通风口面积(A)对车库内氢气的扩散和分布状态的影响。结果表明:在密闭状态下,无横梁时可燃性区域最小,L=3 m时可燃性区域最大;当A=0.5 m2时,在自然通风的作用下,车库底部氢气物质的量分数明显下降,但车库中部和上部氢气物质的量分数与密闭时相近;当A=1 m2时,虽然初始阶段氢气物质的量分数上升很快,但很快就趋于稳定,监测点氢气物质的量分数均在爆炸下限以下,此时自然通风能够消除氢气爆炸的风险。     

海底管道泄漏油气扩散规律数值仿真与对比分析

为研究海底原油与天然气单相泄漏扩散规律的差异性,合理制定应急响应策略,减小事故损失,针对海底管道失效所致的原油与天然气泄漏问题,基于计算流体动力学CFD方法,建立海底油气管道泄漏事故后果预测与评估模型,对特定事故场景下的海底原油与天然气泄漏扩散过程进行模拟与分析,从泄漏扩散过程、工况因素影响、泄漏后果及应对策略4个方面对比原油与天然气的泄漏扩散特性。结果表明:相同工况下,海底原油与天然气在泄漏速率、扩散时间、扩散形态及水平最大扩散距离方面存在显著差别;与天然气相比,原油泄漏扩散行为对工况因素具有更高的敏感性;原油泄漏会引发严重的环境灾害,天然气泄漏则会影响海上结构物的稳定性及引发火灾爆炸事故,据此需合理制定具有针对性的应对策略。     

SBR工艺城市污水处理厂微生物气溶胶逸散特征

在采用SBR工艺的某污水处理厂设置采样点,研究各污水处理工艺段微生物气溶胶的逸散特征.结果表明,各工艺段均有细菌气溶胶逸散,浓度为82～1 525 CFU·m~(-3),粗格栅、生化池和污泥脱水间为主要逸散源.各工艺段检测到的细菌气溶胶主要菌属为Cyanobacteria,其它丰度较高的菌属有Aeromonas、Peptostreptococcaceae、Moraxellaceae、Chroococcidiopsis、Sphingomonas、Arcobacter及Acinetobacter等,其中Aeromonas、Arcobacter、Acinetobacter及Sphingomonas为潜在致病菌.微生物气溶胶的浓度和丰度沿垂直方向和水平方向减少.适宜的温度和相对湿度利于微生物气溶胶在空气中保持活性(P 0. 01),风速则与微生物气溶胶的逸散呈负相关(P 0. 05).污水处理过程产生的微生物气溶胶的暴露风险较小(HQ 1),但是污染物的累积会增加人体的暴露风险.生物除臭反应器在处理臭味气体的同时还可以有效削减微生物气溶胶.     

核电厂大型自然通风冷却塔对气载流出物扩散的影响

为深入研究大型自然通风冷却塔及其湿热羽对内陆核电厂气载流出物扩散影响,应用计算流体力学软件STAR-CCM+提供的k-ε湍流模型模拟了单一冷却塔的运行和停机对不同位置、不同释放高度污染物扩散的影响,结果表明：当释放高度为10m,释放点位于停机冷却塔迎风侧时,释放点下风向的地面轴线弥散因子相比于没有冷却塔时普遍降低1/3~1/2.当释放高度为75m,冷却塔运行时,若释放点位于冷却塔迎风侧时,轴线弥散因子相比于没有冷却塔时普遍增大1~2倍;若释放点位于冷却塔背风侧,则相比于没有冷却塔时普遍降低约1/2.当冷却塔停机时,无论75m高度释放点位于迎风侧还是背风侧,其轴线弥散因子均高于没有冷却塔时.当迎风侧释放高度达到150m时,在释放点下风向约800m的范围内,冷却塔湿热羽使得轴线弥散因子显著增大,但到了800m范围以外,冷却塔湿热羽使得轴线弥散因子减小.     

粉尘在巷道中的紊流传递分析

建立的粉尘在巷道中的传递方程是一个二维平流扩散输运方程。在巷道顶底板为吸收壁的条件下，导出了粉尘浓度分布函数。传统的工业沉降室沉降效率公式（横向混合模型）只是论文所列方程的一个特例。降低紊流强度和减小紊流扩散系数和纵向弥散系数均可提高沉降效率     

Modelling of dust lifting process behind propagating shock wave

Dust dispersion from a layer is a complicated problem, which has not been completely solved yet, especially if an Eulerian–Eulerian approach has to be used to model the two-phase dusty flow. In previous investigation, a phenomenological model of the dust dispersion process from a layer was developed, but the evaluation of the model revealed some weaknesses. In the current paper, the model of the dust dispersion process was presented and three improvements of the model were studied: Saffman force, Magnus force and particles collisions. The implementation of Magnus and Saffman forces into the code did not improve the numerical results and it was shown that it had very little influence on the dust lifting process, in case the phenomenological model of the layer is used. Some explanations were proposed in the paper. Besides, an empirical model of particles collisions was also added to the code and its influence on the results was studied. It was shown that the particles collisions model improved the obtained results, but further modifications are to be studied in the future.     

Quantifying methane emission from fugitive sources by combining tracer release and downwind measurements – A sensitivity analysis based on multiple field surveys

Using a dual species methane/acetylene instrument based on cavity ring down spectroscopy (CRDS), the dynamic plume tracer dispersion method for quantifying the emission rate of methane was successfully tested in four measurement campaigns: (1) controlled methane and trace gas release with different trace gas configurations, (2) landfill with unknown emission source locations, (3) landfill with closely located emission sources, and (4) comparing with an Fourier transform infrared spectroscopy (FTIR) instrument using multiple trace gasses for source separation. The new real-time, high precision instrument can measure methane plumes more than 1.2 km away from small sources (about 5 kg h^?1) in urban areas with a measurement frequency allowing plume crossing at normal driving speed. The method can be used for quantification of total methane emissions from diffuse area sources down to 1 kg per hour and can be used to quantify individual sources with the right choice of wind direction and road distance. The placement of the trace gas is important for obtaining correct quantification and uncertainty of up to 36% can be incurred when the trace gas is not co-located with the methane source. Measurements made at greater distances are less sensitive to errors in trace gas placement and model calculations showed an uncertainty of less than 5% in both urban and open-country for placing the trace gas 100 m from the source, when measurements were done more than 3 km away. Using the ratio of the integrated plume concentrations of tracer gas and methane gives the most reliable results for measurements at various distances to the source, compared to the ratio of the highest concentration in the plume, the direct concentration ratio and using a Gaussian plume model. Under suitable weather and road conditions, the CRDS system can quantify the emission from different sources located close to each other using only one kind of trace gas due to the high time resolution, while the FTIR system can measure multiple trace gasses but with a lower time resolution.     

CFD simulations of dust dispersion in the 20 L vessel: Effect of nominal dust concentration

Measurements of flammability and explosion parameters for dust/air mixtures require uniform dispersion of the dust cloud inside the test vessel. In a previous work, we showed that, in the standard 20 L sphere, the dust injection system does not allow generation of a uniform cloud, but rather high gradients of dust concentration are established. In this work, we used a previously validated three-dimensional CFD model to simulate the dust dispersion inside the 20 L sphere at different dust nominal concentrations (and fixed dust diameter). Results of numerical simulations have shown that, as the dust nominal concentration is increased, sedimentation prevails and, thus, when ignition is provided, the dust is mainly concentrated at the vessel walls.     

Validation of the UK Met. Office’s name model against the ETEX dataset

The ETEX 1 data set has been used to assess the performance of the UK Met Office’s long-range dispersion model NAME. In terms of emergency response modelling the model performed well, successfully predicting the overall spread and timing of the plume across Europe. However, in common with most other models, NAME overpredicted the observed concentrations. This is in contrast with other NAME validation studies which indicate either no significant bias or a tendency to underpredict concentrations. This suggests the reasons for overpredicting are specific to the ETEX situation. Explanations include inadequate vertical diffusion or transport, possible venting by convective activity, and experimental errors. An assessment of a range of advection schemes of varying complexity indicated no clear advantage, at present, in using more sophisticated random walk techniques at long range, a simple diffusion coefficient based scheme providing some of the best results. A brief look is also taken at a simulation of the more problematical ETEX 2 release.     

减推力起飞对NOx排放影响计算方法研究

伴随着航空公司对未来几年氮氧化物(NOx)排放量增长的预测,量化机场NOx排放量日益重要。根据国际民航组织认证的发动机排放数据,在研究推力对NOx排放的影响时,通常模拟4个推力级别:100%(起飞阶段)、85%(爬坡阶段)、30%(进近阶段)、7%(慢车阶段)。美国联邦航空局设计了模型——排放和扩散模拟系统,利用该模型对4个阶段分别进行模拟。结果表明,飞机在最大推力时产生的NOx量最多。分析了起飞阶段减推力下起飞对机场年NOx排放量的影响,通过排放和扩散模拟系统,研究了一系列算法,用于预测推力与NOx排放量的关系。